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Group of administrative and application wide worksheetsR - Reference TablesGroup WorksheetStandard Units ParameterValueUnitsmetersmsecondssec kilogramskgdaysliterslgallonsyearyr cubic feetcu-ftpoundslbspctcountcntcubic feet per yearcu-ft/yrA3 Links Home PageTo A1 OverviewQwft3/year LwMairKETRVVVTLTft3 VBLfgWorksheetLinkOrderCalculator Worksheet ListR2 Reference TablesVPamb g/moleVPambVolume of tank in gallonsMdi PctMolecular weight of MDIAmbient temperature in C .Average day-night temperature fluctuation in CNumberOfProcessesNumber Of Processes ListWorksheetName2Fugitive emissions calculated from monitoring dataKValid Temperature UnitsValidTempUnitsValidVolUnitsValid Volume Units)Fugitive Emissions - From Monitoring Data A4 Guidance7Calculation of emissions from a continuous open process$Calculation of emissions from spillsGuidanceOpen Process ContinuousSpray CoatingEnter value and select units.Temp Range C Min MaxtempRangeCMinMax lb/year-itemKcon itemsEmissions quantityhrs/yr`+Macros MUST be ENABLED to use this workbookLbVPMDI ft2 SCFMMWm/secValidVelocUnitsValid Velocity UnitsACFMLspill ValidWSUnitsmiles/hrhrsft3/yr LspVairdegrees centigradeTotal Emissions1/yrCollection of reference data tables such as vapor pressure of mercury, percent of composition for MDI/PMDI, and other measures.Report Number:Company: User Name:City:Date:State:M1Process Step Type Process No.M2M5M6M7TOTALSTankFugitive - Monitoring DataWORKING LOSSESBREATHING LOSSESTemperature Fluctuation RangeStatusS1 Emissions SummaryGSummary report of all emissions reported by your entity using this tool S - SummaryEmission totals 5http://www.americanchemistry.com/s_plastics/index.aspBGuidance for which calculation methods to use for which operationsEnter value and select unitsAmbient Temperature in C'Adjustment factor to the vapor pressure Temperature of process area in CEnter items in serviceEnter surface area of spill Vapor expansion factor lb-mole/dayTotal air displacedTemperature convertedTspillLconTamb Ambient TemperatureTTamb Storage Temperature Tamb Ambient Temperature !Connectors (e.g., Quick Connects)ft/secValid Density Unitslb/ft3lb/galValidDensUnitsValid Surface Area UnitsValidSurfAreaUnitsStorage temperature in CkelvinValid Volume Units per yearValidVolUnitsPYgal/year-How many sets of monitoring data do you have?ppbv GRAND TOTALConcentration Units ConcUnits"How many sets of data do you have? Data Set #/Enter temperature and select units: F, K, or C.(?Fahrenheit)Valid Wind Speed UnitsReference Pick List Lookup nThe tables are in sets of columns arranged from left to right. Entries for each table are on individual rows. ?Typically, there is a parameter column that displays in a list or combo box, the value column, a units column, and a description or notes column.hPick list lookup table names are in row 13, column names are in row 14, and data values begin in row 15.jThis area contains the collection of pick list lookup tables with their associated values and definitions.Saturated Vapor concentration(Pa)SV (measured)% T (degree F) T (degree C)m2/sDDiffusivity in airTemperature converted to KPaCHART FOR DIFFUSIVITY IN AIRG.MDI vapor pressure based on temperature, in PaPatmPvIdeal gas constantRAtmospheric pressureV!Airflow speed, converted to m/secSurface area converted'Surface area of spill, in square metersAtPa m3 mol-1 K-1   m2 #Air velocity over the spill surfaceft2/sec +gas phase mass transfer coefficient for MDIg/hr#Evaporation rate, in grams per hour=Enter time that the spill is on the ground in hours in a yearmFixed Roof Tank Filling and Storage emissions estimate for working and standing storage (or breathing) losses times/yearKNTank Capacity (VLX)Throughput Volume (QW)UnitlessAnnual Turnover Rate (N))Maximum liquid volume in the storage tank!Calculated turnover rate per year;Working loss turn over factor calculated based on EPA AP-42Volume of Tank (VT)/MDI monomer vapor pressure based on temperatureFPercentage of tank that is liquid-filled. Enter value between 1 to 100SEnter value and select units.(Entire volume of a tank, not to be confused with VLX)PRValve Equipment ModificationSealless designPump Equipment Modification Connector Equipment ModificationValve Control EfficiencyPump Control EfficiencyConnector Control EfficiencyPump ModificationsValve ModificationsConnector ModificationsPumpMods ValveModsConnModsWelded connectionsClosed-vent system No controlDual mechanical seal Kconnector  Ksampling connections 'Emission factor for heavy liquid valvesEmission factor for connectors(Emission factor for sampling connectionsValves in Heavy Liquid Service ConnectorsSampling Connections!Sampling Connections Modification"Sampling Connections ModificationsSampModsClosed-loop samplingSampling Connections EfficiencyKheavy liquid valves "Emissions from heavy liquid valves&Emissions from heavy liquid pump seals#Emissions from sampling connectionsEmissions from connectorsCalculated emissions of MDIlb/hour-equipmentNumber of equipmenthr/yr Kgeneral Pumps/Agitators Seals"Kheavy liquid pump/agitator seals !4Emission factor for heavy liquid pump/agitator seals6Total number of Pumps/Agitators/Pressure Relief ValvesKEmission factor for heavy liquid pumps,pressure relief valves and agitators;Pump/Agitator/Pressure Relief Valves Equipment Modification7Pump/Agitator/Pressure Relief Valves Control Efficiency4Emissions from Pump/Agitator/Pressure Relief Valves Kgeneral &Pumps/Agitators/Pressure Relief ValvesLgeneral7Fugitive Emission from Equipment Leaks (SV is not zero)3Fugitive Emission from Equipment Leaks (SV is zero)<Fugitive Emission from Equipment Leaks (SV is not available)1/hrNhrtohr9Total number of working hours in a year for this building Volume of the workspace buildingEnclosed Process-VolumeCformAEnter number of mold cavity/blend tank/containers filled per year"Enclosed process temperature, in CLenclosed-VolAnnual volume of released airEnclosed Process-WeightoCalculation of emissions from an enclosed process based on the amount of material used and density of products lb/ft3 Enter the density of the productDensity of the product'Enter annual weight of product producedDensity of the raw material+Annual weight of the total product produced"Annual weight of raw material used< (Enter annual weight of raw material usedkrTopenLopen$Airflow speed, converted to miles/hrKx-Evaporation rate without considering reactionkr$Calculated first order reaction rateR'?t Exhaust Air - Monitoring Average exhaust fan flow rateft3/min (CFM) PTotal number of working hours in a year when the exhaust fan system in operating.Enter temperature and select units: F, K, or CLexh.airLexh.satEfgLenclosed-weight5Annual volume of exhaust air saturated with MDI vapor,Calculation of emissions from spray coating Spray gun transfer efficiencySpray booth filter efficiencycEnter spray gun transfer efficiency. For HVLP gun, the minimum efficiency is 65% according to USEPA-If sprayed in an outdoor environment, enter 0@Calculation of emissions from oven during coating drying processVoVolume of oven'Total number of drying cycles in a yearft3Loven0Calculation of emissions from air drying processt1t2ft2/yr ,Air exhaust system filter efficiency, if any?EsLair-dryeEnter the estimated spraying time (starting from mixing the coating and ending when spraying is done)Tair-dryTOTAL emission of the two steps1TOTAL emission of the spraying process (1st step)%TOTAL emission of the oven (2nd step)Ahttp://www3.epa.gov/ttn/chief/eiip/techreport/volume02/index.html"http://www3.epa.gov/ttnchie1/ap42/0http://www3.epa.gov/ttn/chief/webfire/index.html(Overview page of equipment leaks modules3Estimate fugitive emissions when no SV is availableft2/day +Estimate fugitive emissions when SV is zeroft3/year m2/day /Estimate fugitive emissions when SV is not zero'Overview page of the enclosed processes/Estimate emission when material weight is known7Estimate emission when container/cavity volume is knownM5 Open ProcessM5a Open ProcessKEstimate emission from open process with the consideration of reaction rateM6 Exhaust Air-Measured<Estimate emission from measured concentration in exhaust airM6S Exhaust Air - SaturatedEstimate emission from spill;Estimate particle phase emission from spray coating process.Estimate vapor phase emission from drying oven2Estimate vapor phase emission from air dry processM2 Fugitive_Monitoring DataM3 Fugitive_Equipment LeaksM4 Enclosed Process_OverviewM4a Enclosed Process_WeightM4b Enclosed Process_VolumeM6S Exhaust Air_SaturatedM6 Exhaust Air_MeasuredM3a Fugitive_Leak No SVM3b Fugitive_Leak-SV is ZeroM3c Fugitive_SV is not zeroM3a Fugitive No SVM3b Fugitive SV is ZeroM3c Fugitive SV is not zero' M3a Fugitive_Equipment Leaks_No SV- M3b Fugitive_Equipment Leaks- SV is Zero0 M3c Fugitive_Equipment Leaks_SV is not zero M4a Enclosed Process_Weight M4b Enclosed Process_Volume M5a Open Process M6S Exhaust Air_SaturatedM5 Open Process OverviewBOverview page of the open processes and calcuate the reaction rateOpen Process - OvenTOTAL of Oven Drying/CuringLopen process total?Enter molar % of MDI/PMDI in the formulation, 1-100, 100 if only MDI/pMDI exists, weight % can be used if it is close to molar %M3aFugitive_Leak No SVM3bFugitive_Leak-SV is ZeroM3cFugitive_SV is not zeroM4aEnclosed Process_WeightM4bEnclosed Process_Volume Open ProcessExhaust Air-MeasuredM6SExhaust Air - Saturated?Calculation of emissions from using MDI/pMDI as a binding agentBinding AgentTank Emissions.Calculated volume of vapor space (VV = VT-VLX)#$ () +-EPA default control efficiency?Select modification type, if applicable, or select "No Control"toptop TEmission factor for heavy liquid pumps, pressure relief valves, and agitator seals WCalculation of emissions from an enclosed process based on the volume of enclosed spaceJCalculation of emissions from curing/drying oven following an open process Loven total Lopen totalLenclosed-Vol totalLenclosed-weight total Efg total Lfg totalQecLexh.air total;Average flow rate of the exhaust fan of the control measureLexh.sat total%Air velocity over the product surfaceTopLbinding agentLbinding agent total)Surface area of product, in square meters Lspill total#/yrLspray coating total Lsp subtotalLair-dry subtotal% MDI in MDI/PMDI (KMDI)(?g/m3)7Enter temperature in oven and select units: F, K, or C.Lba_openLba_open total!Enter values in yellow boxes only?Enter molar % of 4,4' and 2,4' MDI monomer in MDI/PMDI, 1-100, weight % can be used if it is close to molar %. Contact supplier if not sureoft2/year ?Enter surface area of product produced per year, do not include surface area which is not exposed to air, e.g., the bottom area of a foundry on conveyor or foam surface covered by other materials?Enter values in yellow boxes only, if you do not have the required information, ignore this page and go to M5a and the default reaction rate is provided"AAir velocity over the product before curing (e.g., on a conveyor)@Enter value and select units (typical indoor velocity: 1-3 ft/s)?Enter time when the product is exposed to air, e.g., starting when MDI is mixed with sand and ending when a foundry is placed in an oven. It can be estimated using the length of the conveyor (ft) divided by its speed (ft/hr)3Air velocity over the product surface while air dry,Step 2: Open Process at elevated temperatureYStep 1: Open Process at room temperature (MDI/pMDI is mixed with the substrate materials)TOTAL of the 2nd step L2nd StepFilter Efficiency?Enter surface area of product produced per year, do not include surface area which is not exposed to air, e.g., the bottom area of a foundry/particle board on conveyor or foam surface covered by other materialsvEnter temperature and select units: F, K, or C. (Default value is 200 F, please fill the temperature at your facility)0 ?Enter time when each product is exposed to high temperature, e.g., the time that OSB or particle board stay in the press room or the time that hot metal stays in the foundary (typical value is 0.05 hr) ? uEnter control equipment efficiency for the elevated temperature step, if no control, enter 0 (Typical value is 99.3%)] Spray ListM7 SpillM8 Spray CoatingM8a Spray Coating_OvenM8b Spray Coating_Air Dry M8a Spray Coating_Oven M8b Spray Coating_Air DryTDI Emission Calculator>Collection of reference data tables such as vapor pressure TDIM8*ACollection of reference data tables such as vapor pressure of TDIVPTDIKTDI;the vapor pressure of TDI in mm Hg. at process temperature.ythe adjustment factor to the vapor pressure that is a function of TDI concentration in the feedstock and the temperature.molecular weight of TDI (174.2)<Annual throughput of TDI pumped to the tank in ft3 per year1 4/Calculated emissions of TDI from working lossesMolecular weight of TDI9Adjustment factor based on temperature and percentage TDI1Calculated emissions of TDI from breathing losses&Calculated emissions of TDI (combined)'TDI vapor pressure based on temperatureCtdiMolecular weight of TDI Calculated emissions of TDIiEnter total time that the process or equipment is operating (i.e., in contact with TDI or TDI Prepolymer)3Calculated total emissions of TDI or TDI PrepolymergEnter total time that the process or equipment is operating (i.e., in contact with TDI/TDI PrepolymerI)!Calculated total emissions of TDIfEnter total time that the process or equipment is operating (i.e., in contact with TDI/TDI Prepolymer)STDI emissions from heavy liquid pumps, pressure relief valves, and agitator seals TDI emissions from connectors5M. Group of worksheets for Estimating Releas<ves of TDIDEstimate emission from exhaust air assuming saturated with TDI vaporMolecular weight of TDI isomer.TDI isomer vapor pressure based on temperature>Weight percentage TDI isomer in the TDI/TDI Prepolymer mixtureMWTDIVPTDI ?Enter molar % of TDI isomers in the formulation, 1-100, 100 if only TDI isomers exist, weight % can be used if it is close to molar %IEnter the density of the raw material (TDI isomer density is 75.5 lb/ft3)G H/TDI monomer vapor pressure based on temperaturevEnter molar % of TDI in the formulation, 1-100, 100 if only TDI exists, weight % can be used if it is close to molar %zThe amount of time from TDI starts to react to the time when the remaining non reacted TDI reaches R' (%) as entered above>% of TDI is not reacted at a specific time ?t as entered belowvEnter the estimated curing time (starting from mixing TDI with polyol and ending when the product is considered cured)YEnter the estimated first order reaction rate of TDI with polyol, default value is 7.2/hr+gas phase mass transfer coefficient for TDINSurface area of TDI containing product manufactured annually, in square meters.TDI vapor pressure based on temperature, in Pa8Evaporation rate without considering reaction and filter8Calculated TDI emissions considering reaction and filterExhaust filter efficiencyg/yr5Annual volume of exhaust air saturated with TDI vaportProcess emission calculated from measured airborne TDI concentration in exhaust air of controlled ventilation systemYAverage measured TDI airborne concentration from exhaust vent ( enclosed production line)RCalculate process emission by assuming the exhaust air is saturated with TDI vapor%% TDI isomers in TDI feedstock (KTDI)!$?Enter molar % of 2,4' and 2,6' TDI isomers in the TDI feedstock, 1-100, weight % can be used if it is close to molar %. Enter 100 if only isomers exist. Contact supplier if not sure?KTDI ?Enter molar % of 24' and 2,6' TDIisomer in the TDI feedstock, 1-100, weight % can be used if it is close to molar %. If only TDI isomers exist, enter 100. Contact supplier if not sure?Total weight of TDI sprayedwAnnual amount of TDI sprayed. Note: enter the amount of TDI only, do not enter total amount of coating material sprayed!% TDI in the TDI feedstock (KTDI) ?Enter molar % of 2,4' and 2,6' TDI isomer in the TDI feedstock, 1-100, weight % can be used if it is close to molar %.If only TDI isomer is used, enter 100. Contact supplier if not sure?OEnter total surface area of products sprayed by TDI containing coating per yearJCalculated TDI emissions during air dry with the consideration of reactionTDI Emissions Exhaust filter efficiency, 0-100TPercent TDI isomers in the TDI/TDI Prepolymer mixtures. Enter value between 1 to 100Percentage TDI isomersMWOVolume of the cavity/blend tank/container which is not occupied by raw materialPTDI8Annual throughput per year. Enter value and select units Number of air exchanges per hourZAverage TDI airborne concentration within the building. Enter value and select input unitshEnter the measured SV (TDI concentration in the vicinity of any leaking material at the leak interface) ?Enter volume of released air in each container (note: not the volume of the entire container but only the volume not occupied by raw material)puIEnter percentage of TDI in the formulation, 1-100, 100 if only TDI exists?* Note: Emission of spray coating comes from two steps: M8 (Overspray) and M8a/M8b (Drying). The number shown is the total emission of the overspray and drying.? C"? FSVScreening ValueHVLPHigh Volume Low PressureTDIToluene diisocyanate.Enter number of pieces of equipment in service+Number of mold cavity/blend tank/containersdEnter the air drying time (starting from the spraying is done until the product is considered cured),Calculated TDI emissions during air dry step)TOTAL emissions of the air dry (2nd step) TOTAL emissions of the two stepsEPAEnvironmental Protection AgencyKEPA Emission Inventory Improvement Program (EIIP), volume II: point sourcesCEPA AP 42, 5th edition, volume I: stationary point and area sources>EPA WebFIRE: online database of CAPs and HAPs emission factorsExhaust Air - Saturated ?b0? x?T???6?????[??_?????V?2??????????nZ?6????t???p?L ;? ?[ Q?- v?R ?? ?????o7???i?????z=? ??;?????????6?4??????~??????????????N???%????? ??C????R??? ??? ??? h?"?????W'????????<?a?Q? __ ? ??v???N?>? l ,??OB?cc??B??????? ??H9qiZ?E??? ZO?? 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F!Ə??2?f̹?K???m??? ? ?nÕ?{ ?5??(?ZV?J???|????s??k?|;?/?a??!??????[Content_Types].xmlPK-!1?_a?? ._rels/.relsPK-!?-??;)drs/shapexml.xmlPK-!0xs"? drs/downrev.xmlPK?l ???c?]D`???L<? Introduction The TDI emission calculator provides a convenient method to estimate TDI emissions from typical process activities. The calculator has built-in formulas to estimate emissions for the processes listed below. The source of emission estimation algorithms used in this tool are from the United States Environment Protection Agency (EPA) emission reporting guidance such as the "Emission Inventory Improvement Program" and "Emission Factors & AP 42." When the USEPA guidance is not available for certain applications or processes, engineering calculations are used. Please review the guidance and calculation details in each module before using it. You can access this information by clicking "Show/Hide Guidance" and  Show/Hide Calculation Details on each page. Due to the inherent uncertainty in emission estimates using modeling techniques, the numbers estimated in this tool may not accurately epresent the exact amount TDI emission at your facility. If you have measured or monitoring data, use thatfirst. M6 provides a template to use measured data. This calculator aims to provide quick estimates when measured or monitoring data is not available or not feasible to obtain. Please click "Go to Guidance Page" on the right to start You must enable macros in order to use this workbook. This calculation tool requires the use of macros (executable code embedded within a workbook). Please make sure to use the following security settings to allow the macros to function properly: " Microsoft Excel: Click "enable content" on the yellow bar shown on top of the page. 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The American Chemistry Council, the Center for the Polyurethanes Industry (CPI), and its members disclaim any liability that may accrue in relation to, and in reliance on, the scenarios and estimates associated with the model and report. The scenarios that have been selected are thought to be representative of situations where releases may occur. Other scenarios not represented in the report may involve releases as well. It is the responsibility of any manufacturer, processor or user of any listed chemical to know and understand the reporting obligations in accordance with the provisions of the law. Such a manufacturer, processor or user should consult its own legal and technical advisors for specific advice applicable to its facility. The American Chemistry Council (ACC) represents the leading companies engaged in the business of chemistry. ACC members apply the science of chemistry to make innovative products and services that make people's lives better, healthier and safer. ACC is committed to improved environmental, health and safety performance through Responsible Care?, common sense advocacy designed to address major public policy issues, and health and environmental research and product testing. The business of chemistry is an $801 billion enterprise and a key element of the nation's economy. It is the nation s largest exporter, accounting for fourteen percent of all U.S. exports. Chemistry companies are among the largest investors in research and development. Safety and security have always been primary concerns of ACC members, and they have intensified their efforts, working closely with government agencies to improve security and to defend against any threat to the nation s critical infrastructure. Copyright ? March, 2016, American Chemistry Council. <X@ A A?A?AhAiAjA?A?A?P>?@U??? ?? ?? ??##???y??????K? R1 Reference Lookups'R1 Reference Lookups'!A1??$$???y??????K? R2 Reference Tables'R2 Reference Tables'!A1??%%???y??????K? S1 Emissions Summary'S1 Emissions Summary'!A1?b ???y??????K?  A2 Glossary'A2 Glossary'!A1?V ???y??????K?  A3 Links'A3 Links'!A1?b???y??????K?  A1 Overview'A1 Overview'!B9?R ???y??????K? M1 Tank'M1 Tank'!A1?????y??????K? M2 Fugitive_Monitoring Data!'M2 Fugitive_Monitoring Data'!A1?????y??????K? M3 Fugitive_Equipment Leaks!'M3 Fugitive_Equipment Leaks'!A1?????y??????K? R1 Reference Lookups'R1 Reference Lookups'!A1?????y??????K? R2 Reference Tables'R2 Reference Tables'!A1?b ???y??????K?  A4 Guidance'A4 Guidance'!A1?????y??????K? S1 Emissions Summary'S1 Emissions Summary'!A1?????y??????K? M4 Enclosed Process_Overview"'M4 Enclosed Process_Overview'!A1?????y??????K? M4a Enclosed Process_Weight!'M4a Enclosed Process_Weight'!A1?????y??????K? M4b Enclosed Process_Volume!'M4b Enclosed Process_Volume'!A1?????y??????K? M5 Open Process'M5 Open Process Overview'!A1?????y??????K?  M5a Open Process'M5a Open Process'!A1?????y??????K? M6 Exhaust Air-Measured'M6 Exhaust Air_Measured'!A1?????y??????K? 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The structure of this calculator is: M1 to M3 (M3a to M3c): Emission from storage tank and fugitive emissions. M4 (4a and 4b) and M5 (5a): Most TDI isomer applications can be classified into these two categories. Standard emission estimate models are applied. M4: Enclosed process may include the following applications: Reaction Injection Molding (RIM) Molded foam parts (automotive and furniture) Cast elastomers (shoe soles, packaging, furniture) Pour-in-place (appliance insulation, marine products) Filling/mixing/blending in a closed vessel or container M5: Open process may include the following applications: Slabstock/Bunstock Laminate boardstock Metal skin panels Carpet backing/flooring/coating Belt and Tire Cord Bonded foam production Spandex M6: If M4 and M5 do not contain your application or you believe the modeling algorithm does not apply to your process, M6 provides a template to use exhaust air sampling data if they are available. 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D?q/)drs/shapexml.xmlPK-!RA????drs/downrev.xmlPK?! ? ?]?`???kx<lCalculating Working Losses from Storage Tanks Working losses occur when MDI/PMDI vapor that is present over the liquid in a storage tank is displaced from the tank by the addition of MDI/PMDI liquid during tank filling. A reasonable worst case estimate of working losses can be made based on the size and number of storage tanks, the average storage temperature, and the number of times each tank is filled in one year. The working losses can be estimated from the following expression: Lw = Qw * (1 / 359) * (273.15 / Tamb) * (VPamb / 760) * Mw * Kmdi Where: Lw = the working losses in lb/year. Qw = the annual throughput of MDI pumped to the tank in ft3/year. Tamb = the ambient temperature in K. VPamb = the vapor pressure of MDI at the ambient temperature in mm Hg. Mw = the molecular weight of MDI (250.26). Kmdi = the adjustment factor to the vapor pressure . <x?.A?A?A?A???E???E?? 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D??*q읦??f[??H*}??e?T?u?^j|ˍU?#ڂ ˏ?j? ?U???P?LK????A????S'Vz?3?n??,d?񡙼??Wq?????nQ=m.?6n*?????Ă;/-܇kq)$8??':+?=?sk???`$3u?E?繓?%??P??@?Fo??B8?E??7?aE>zێp?????PK-<$!??????[Content_Types].xmlPK-!1?_a?? ._rels/.relsPK-!f???o)drs/shapexml.xmlPK-!?o?<?Edrs/downrev.xmlPK?????]?`<??C <D This worksheet calculates emissions from fixed roof tank described in the EPA Emission Factor Documentation for AP-42 Section 7.1: Organic Liquid Storage Tanks Final Report (Sep 2006). Based on section 3.1.1 of the aforementioned document, total loss from fixed roof tanks includes standing storage losses (or breathing losses) and working losses. Simplified equations have been developed to calculate these losses due to the tedious and time consuming process of following the EPA detailed method. Case studies demonstrate that the discrepencies low volatile chemicals (less than 30 mm Hg) between the simplified method vs. EPA method are within 2~3% and 10% for working losses and breathing losses, respectively. Due to the very low vapor pressure of TDI, it is assumed these simplified equations apply. A detailed explaination of this method can be found in Jimmy Peress, Emission Storage Tank Emissions, CEP Magzine, American Institute of Chemical Engineers. Aug 2001, page 44-45. One modification made to Peress, 2001 is the annual turnover rate which is adopted from the aforementioned EPA AP-42 documentation, equation 3-30. The working losses can be calculated as: L_w=(Q_w?MW?K_N)/359?273.15/T?VP/760?K_TDI Where, L_W = Working loss (lb/yr) Q_w = Annual net throughput (ft3/yr) MW = Molecular weight (lb/lb-mol) K_N = Working loss turn over factor, dimensionless, for turnover (N) > 36, K_N = (180+N)/(6?N), for turnover < 36, K_N = 1, N = Annual turnover rate (1/yr), N = (5.614?Q_w)/V_LX , V_LX is the tank maximum liquid volume (ft3) T = Temperature (K) VP = TDI isomer vapor pressure at temperature T (mm Hg) K_TDI = Weight fraction TDI isomer in the TDI isomer/TDI Prepolymer mixture (unitless), enter 100 if only isomers exist The standing losses or breathing losses can be calculated as: L_s=(365?V_v?MW?K_E)/359?273.15/T?VP/760?K_TDI Where, L_s = Standing storage loss (lb/yr) V_v = (V_T?(100-L_T))/100, vapor space volume (ft3/yr), V_T = Volume of the tank (ft3), L_T = Percentage of tank that is liquid-filled (unitless) MW = Molecular weight (lb/lb-mol) K_E = T_R/T, vapor expansion factor (unitless), T_R = Day-night temperature fluctuation (K) T = Temperature (K) VP = TDI isomer vapor pressure at temperature T (mm Hg) K_MDI = Weight percentage TDI isomer in the TDI/TDI Prepolymer mixture (unitless), enter 100 if only prepolymer exists <HoIpH?I?J?J?J?J?J?J?J?K?J?K?J?J?J?J?J?K?J?J?J?K?J?J?J?K?J?J?J?I?H?I?J?J?J?H?H?J?J?J?ILI H,I-J.J/J0HyJzJ{J|HJ?J?J?J?J?J?J?I?J?J?J?H?I?J?H?J?J?K?J?J?J?J?J?J?J?J?H?J?J?J?HMHH$I%H]J^J_JbI?I?I?I?IJJJJJKJJJ K!J#K$J%J&J'J)J,K-J3J4J5K6J8J9J<K=J>J?JBICIJJKJLJMI`InJoJpJqItJuJvJwJxKyJJ?J?J?J?I?I?L?I?J?J?J?H?M?H?J?J?J?H?IH!I"J#J$J%I(J)J*J+J,J-IRJSJTJUH}I~I?I?J?J?J?H9 H@ IA IB IC <??? ??? s ?Z?A" ??@???0Combo_worksheetLinkList?BJ?]h? 1 > Forms.ComboBox.1T #< ? !? ??x ? ?P?X?C^???????????????TextBox 9"? ?À PK!??????[Content_Types].xml???J?0????*m?i??G]`H?m?6 ?Xw??t?.? g???#?W?i3E??)?.+?7?? >?O?N? ?ޑ?1??ˋz? ?"?+R ?R?hB.} ?/???????0???x??M ??e??`??|X}?????đ ?I`߽??N4a?G2?$?R?KI?Z?)?4?(?M?9`?ctB{????m?:?f@?`??3??n?|O?????,ܗ?r???޾?j??x??R0T ?,?0????@?????}W?B?L??Ǭ5v??PK!?ֹ?1mdrs/shapexml.xml?]?n#ɕ?0? ?,Q?(?TtI?JU?Ӟz%ٽ3?dN僝??Z6?F??Mɛ^h???????????܈?#I?d&?$?R??Ɍ׽?޸?x????+FN????J? ? l?o?~u?r??"?}???/?K7"*??????i??ܷ?A?? ????q?-e???Ym??t???? ???װ?k??/??ݽJ?p7ꄂ?Q[?\?)??w???L??jB_j????Y?{Ry?K}??????<9????芺?'??2}?_?????????=???a{2???x??ju?vw?{?h???vxW?Ԛg?O])B?Kq?R?2?gϺ?4{<|???X????i8?#oԌcz??v?X"~#??O??s?0???,??A????k??T+?w?{'??:???KxK?tQ?y??.??=?:?{|?S?_]t??x:?\??̱Ax?;?{ ?K??Y?cOJ????L?pO?u?.IQn$/??Y;???-4Q1B??EǢ?Q?:????*q???l$(x]??$???????Z?0~??+O.?NĮ??R&??]??BzFLxND?M?H????6 ???=?B??4?<f?R?V??g????i୎?d[?|??cy????????^rKB?zX]?2w??????m]?#??Q?=?t? ???????r?a^i8z ??x̎G??d ??? ?\???h?]??;?+??빅ih@m?m??/>?j???????:??t?>?5?k?+?B?X?+?B+?ѧ!?P?#???]AwiDR?NЍTK???@S]?H ?9???7ѫ??,?͠?w???57e?|????F??h ?p???m?H\???)???-y?Co?Kz? ?i?S/K??H?:? ?r??|?!????,?jC???f?/ϻa?d{(?F???*8{q?^??y??N=?|??IGv?"????? ???`??t[$??۬CBpg??????y?j`??T?z???"Tb%??]H(?}??Z5?]???h?:Z?P?'%A???}????? 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Edr?h8.[ᰐtb???????r#]lV???D%???Z?u??>????]W1?.?ƥ?؞??6??X[???ވ??Vm?#W5???#W??\m???6j?? ??+g??1?s?.?궚??~???.wء2?AOif?Zy?˕? m|O?s?????y???hf??x???#*,9?P `?{?_m^???J*?4 }?E??UdqP?1e???T>`qO????9?z!M%?Jn?:BQ????T??????$et??U(X??+??ΞK_????PK!?y??drs/downrev.xmlT?[k?0?????f??C?tF)?T u??iz?&)I?u?~_ ??˓??L獪?QZW͠? ?H-LZ?????s?y?S^-??????n??Ԝ?Vw>'?]???1?NRq?3??????G?9M-?a??? ?T?RcC?k?(?8?~??B}=?cq-6?(YFnsHc?M????_?˷????מּ??u?`<?@??yo?t˝??N??8f???- c?sf?"֜?D???"?g???#??PFQm????M??o|??$?l?????????PK-!??????[Content_Types].xmlPK-!1?_a?? ._rels/.relsPK-!?N&?r ?o)drs/shapexml.xmlPK-!?y???drs/downrev.xmlPK??03?]k `?????<c Fugitive emissions are non-stack emissions that escape during material transfer, from buildings that contain the process, or directly from process equipmeocess emission estimate uses the method listed in the EPA Emission Inventory Improvement Program (EIIP), volume II: Chapter 8, Methods for Estimating Air Emissions from Paint, Ink, and Other Coating Manufacturing Facilities (USEPA, Feb, 2005). Please refer?????????????????????????????????????????????????????????????????????????????????????????????????????????????????????????????????nt (As defined in the summary of the EPA Method 22). This worksheet calculates fugitive emissions from buildings that contain the process only. For fugitive emissions from equipment leaks, Rfer to "M3 Fugitive-Equipment Leaks." Fugitive emission from buildings that contain TDI related process can be estimated by direct measurement or monitoring data (e.g., TDI airborne concentration in building exhaust air). In the absence of direct measurement or monitoring data, industrial hygiene data on TDI concentrations in the workplace can be used to estimate TDI isomer fugitive emissions. This technique can only be used if the industrial hygiene data are representative of average concentrations throughout the building during working hours. This method assumes a constant ventilation rate during working hours and uses average airborne TDI concentration to estimate fugitive emissions from buildings. Note to include both fugitive emission and stack emission from a specific process. For example, if a TDI using process is enclosed by a tunnel which has an exhaust fan, be sure to include the emissions from the tunnel exhaust fan using M4, M5 or M6 in this tool in addition to emissions from the building general ventilation. Do not double count the TDI emissions. For example, if a factory building has a TDI using process which is not enclosed, emission calculations using the general building ventilation have already included all the reportable TDI emission in that building. Do not use any other modules in this tool, otherwise the emission will be double counted. Consult CPI for any questions. The fugitive emissions can be estimated from the following expression: L_fg= C_TDI/(1,000,000)?V_B/359 ?N_hr?(273.15)/T_amb ?0MW0_TDI?t_o Where: Lfg Fugitive emissions (lb/year) Ctdi = Average TDI concentration in the air within the building (ppmv) VB = Volume of the workspace building (ft3) Nhr = Number of air exchanges per hour (1/hr) Tamb = Ambient temperature (K) MWTDI = Molecular weight of TDI (174.2) to = Total number of working hours (hr) <??H?P?Q?P?A?A%A&?*R+R,R0R1R2R3R6R8RARBRCRDRERFRGRLRMRNRORQRRRSRYR[R\R]R`RaRbRcReRfRgRjRkRlRmRnAoApAwAxFzA?A?F?A?A?F?AG A A FA9A:F>AXAZF^A?H?S?H?I?A?A?A?A?A?A?A?A?A????? ?? s ?V?A, ??@???,cmd_calc1_clearValues?S!q?#?]`? 1 6$Forms.CommandButton.1TL???? ?? s ?X?A5 ??@???.cmd_calc1_showHideCalc?? ?]`? 1 6$Forms.CommandButton.1?`???? ?? s ?X?A ??@???.cmd_Number_Sets_Select????!??]`? 1 6$Forms.CommandButton.1H???? ??? s ?X?AC ??@???.cmd_calc1_showHideGuid??S?]`? 1 6$Forms.CommandButton.1HT???? ?f? s ?Z?A ??@???0Combo_worksheetLinkList?B?J?]hf 1 > Forms.ComboBox.1?h #<[?[? ?l? ? ?h????C^?(k?(k??????????????TextBox 1"??ãPK!??????[Content_Types].xml???J?0????*m?i??G]`H?m?6 ?Xw??t?.? g???#?W?i3E??)?.+?7?? >?O?N? ?ޑ?1??ˋz? ?"?+R ?R?hB.} ?/???????0???x??M ??e??`??|X}?????đ ?I`߽??N4a?G2?$?R?KI?Z?)?4?(?M?9`?ctB{????m?:?f@?`??3??n?|O?????,ܗ?r???޾?j??x??R0T ?,?0????@?????}W?B?L??Ǭ5v??PK!?ڻ???Pdrs/shapexml.xml?\mS?8?~U?T???y#?lj??,3\M??P {?Y??ąly$?$???i9???08l00I???V????|@?е?6??B=?+F????u???Oƒ??.?Y????HʿC F?G?R?k.??{?YHg?n?O?.??Ǵz?δ2?H}????&V??.??lD?'h??AH?sarg+>????f??1?Dr????tF?auʲ??`???HGW??pG?????s9s+??'?$?Q??<!?A??h?#?|s{ ??? {r??#] ?!? ?????`?c?J"?4?r??8e?????[???DA??=?$8皓u???*!????8k????Ɂ?9?_75~ ??7 ?? zQ???@r??ѿb?y;? ??T? s΀|P?Kf5OL(?>?,?tx??!?9;?/??gH9???P9g??-L|ˢ4?e{?{L?\ϙ ????ga'*`??Cv9? ?*}?P?s?gЗ0,,\???uU????c*??Cv.o?٭ؔ?_A???`Z@?*?}?"?|(??DW{ ??[N?;?]???$UP*??  ??Fd???? ???dZ8-B????'LJ????H??Nɇ?5¨J(‘??l?3c?*(za>2?]2Gn?t?j?8?L??H?;G??ҵ)?&???u?f2B????^H-"?IH??Ͻ4Q?_t{??R6_e`?PO??#b?c88?L Y?7?A??G1J|?e?c&~F~E?Dp???Щ?"??@?*%?E???T?s??Kt??JĦN:^?u6????,?J}??2i???G ????IZ?p???3?)?????*9?#?Aj???J?F3????a??&OZ?e?t??pKl?1?`Cn*??&Ex1??????{?r ???9n?w??r???L?>?V???N???c??)? nk!o[??cCv?m?6 ??m?ؠ[?}???_???-i???}?6hJ?b????`?/ۖ?i3N??%lҎp??q?ӇE/?-hӦ??h?"6hK???ۖ?iN?-`??????֫X" ???׆Q?҂?/5X?Q?k?e?U/???hZݟ?'??uhT??;?Þ?|?????????;t?[???6??y-?X?Of-????U?ֲ?????lֲ?I?d?7t?[????5\?Z?,{тf???Kr???A?i'?h?????{YQǿY?_l4A?%jT??}'E=???i|?d?g?;6X+??Ҧq???z6??JbCN???m?Ki?U?n?s?zZ@??d}??2?߫YO???d??Ϝ?lP??????&Řz6?B?p???$?GؒG?;??????2,?Iڳ??:??n???~?joֶz??????:?K???!?-?oE ?????Of@????6?g? ?M;???W????b0???"?l4_??/c?뉔?j̣??x?5?ƹ ?z?6?gp??2e? Z???>L??????|$s???e???=M??k.W\搜??*???C?u????V?w???M!??~??ƞ*ߡ~???,>WQ??av???w?G|??_*_?%???z???z&s?]?w?u+޼?~??Ƚ?O???{???6!љ????s?[?N???PK!?*7?$?drs/downrev.xml\??N1??M|?fL??.K\~?$71h@?ۺ????V?}{?`??9?̜ǵ??V;_??nE???P?v-??uv?惴JVh??F{?./?r?pgz? kFC?HE??>+????m???32?tk????pS?8?ndiiC!7zZ??k?m???w?~??ýM?????c&??U=?t??yʛ9??D?N?øT ?????ӕj!}?N壴?F??&6+??߹C??$?2?^??y?u "?F??:??~?6???N??¾prvz??B,?{??~??PK-!??????[Content_Types].xmlPK-!1?_a?? ._rels/.relsPK-!?ڻ???P)drs/shapexml.xmlPK-!?*7?$?G drs/downrev.xmlPK?? ?F?==?]l `<??{?<|Fugitive Emissions - using monitoring data in a building Fugitive emissions are non-stack emissions that escape during material transfer, form buildings that contain the process, or directly from process equipment (In the summary of the EPA Method 22). This worksheet calculates fugitive emissions from buildings that contain the process only. For fugitive emission from equipment leaks, please refer to "M3 Fugitive-Equipment Leaks". 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The screening value (SV) is a measure of the concentration of leaking compounds in the ambient air that provides an indication of the leak rate from an equipment piece, and is measured in units of parts per million by volume (ppmv). The source screening procedure should follow the EPA's "Protocol for Equipment Leak Emission Estimates (1995)," section 3. When a SV is available, the EPA "Correlation Approach" is preferred. If no SV is available, please click "Back to Fugitive-Equipment Leaks Main Page" below and select the "Average Emission Factor" approach. Table 2-9 in the aforementioned protocol, section 2.3.3, page 2-26 presents the correlationship between leak rate and SV. The relevant equations for TDI manufacuting are below: Kgeneral = 2.205?1.90 x 10-5 ?(SV)0.824 Kcon = 2.205?3.05 x 10-6? (SV)0.885 Where: SV = Screening Value of TDI concentration of the leaking equipment (ppmv ) Kgeneral = Emission factor for heavy liquid pumps, pressure relief valves, and agitator seals (lb/hr-equipment) Kcon = Emission factor for connectors in (lb/hr-equipment) Emissions for each screening type can then be estimated from the following equations: Lgeneral = Kgeneral ? ngeneral? tpr Lcon = Kcon ? ncon ? tpr Where: Lgeneral = Annual losses from heavy liquid pumps, pressure relief valves, and agitator seals in (lb/yr) ngeneral = Number of heavy liquid pumps, pressure relief valves, and agitator seals Lcon = Annual losses from connectors in (lb/yr) ncon = Number of connectors Ktdi = Adjustment factor to the vapor pressure (unitless) tpr = Total time that the process is operating (hr/yr) Total emissions can then be estimated from the following expression: Etot = Lgeneral + Lcon <?HHHHgHhH?N?N?H9H?N?S?N?aN b aNSNbNS N'a(N1b3a4N7S8N9b?HFH?H?S?H?HIHcH.H>I?N@H?I?N?S?N?S?N?a?N?S?a?N?S?N?N?S?N?S?N?a?N?S?N?R?N?S?I?H?H?H?S?HH@HJHKHLSSH`H?H?H?c?H?H?H?c?H?H?H?c?H&H'H(c+H]H^H_H?H?N?S?N?S?N?S?H?H?A?A?A?A????? ?? s ?V?A ??@???,cmd_calc1_ClearValues?o&:1&??]` 1 6$Forms.CommandButton.1(L???? ?3? ? ?^?? 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If no SV is available, please click "Back to Fugitive-Equipment Leaks Main Page" and select the "Average Emission Factor" approach. Table 2-9 in the aforementioned protocol, section 2.3.3, page 2-26 presents the correlations between leak rate and SV. The relevant equations for MDI manufacturing are below: Kgeneral = 2.205*1.90 x 10-5 *(SV)0.824 Kcon = 2.205*3.05 x 10-6 *(SV)0.885 Where: SV = Screening Value of TDI concentration of the leaking equipment (ppmv ) Kgeneral = the emission factor for heavy liquid pumps, pressure relief valves, and agitator seals (lb/hr-equipment) Kcon = the emission factor for connectors in (lb/hr-equipment) Emissions for each screening type can then be estimated from the following equations: Lgeneral = Kgeneral * ngeneral* Kmdi * tpr Lcon = Kcon * ncon * Kmdi * tpr Where: Lgeneral = the annual losses from heavy liquid pumps, pressure relief valves, and agitator seals in (lb/yr) ngeneral = the number of heavy liquid pumps, pressure relief valves, and agitator seals Lcon = the annual losses from connectors in (lb/yr) ncon = the number of connectors Kmdi = the adjustment factor to the vapor pressure (unitless) tpr = the total time that the process is operating (hr/yr) Total Emissions can then be estimated from the following expression: Etot = Lgeneral + Lcon <xUUUgUhU?T?T?U/U?U?T?W?T?dTWTd TWT%d'T+W,T-d3U4U;U?U?W?U?U?U?U?YU*U:U;T<U?U?T?T?W?T?W?T?W?T?W?T?W?T?T?W?T?W?T?W?T?W?T?W?U?U?U?U?U?W?UUPUZU[U\WcUtU?U?U?Y?U?U?U?Y?UU U YUFUGUHYKU?U?U?U?U?U?T?W?T?W?T?W?U?U?U?U?U?>?@U??????+,9:;<GHIJUV-.WXcdefqrst????????????????? ??????{+{???h???y??????K? 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Ph??ĥ;KwJ-|?b?~HK??a?-"?{.e??w) ???L??MTp??s??? ??Q??`??[??ի?t4o???f? ??yQ?? ???6O??=t?Yl0Ϡ??? ?i? ??z?G?kYʵ??^?OW???ψ??vG?lt`O?I?{ю????;???=?X?>?T?Z/:???]Zz;???|7??*?˅e??U1? rޛ~??Rk??4??n?1?????5?N??bS??B?$*-?9ιђ?gp$?M?E???V?^?????0??A??b??????p??u?ߌ???PK-!??????[Content_Types].xmlPK-!1?_a?? ._rels/.relsPK-!???[? ??)drs/shapexml.xmlPK-!B??v?=drs/downrev.xmlPK???M??] `?????<? The engineering calculation used to estimate TDI emission from enclosed process corresponds to the total volume of air released from the enclosed space at the operating temperature. This method assumes the worst case scenario that the volume of air released is saturated with TDI vapor. Volume of air released is defined as the volume which is not occupied by TDI in the enclosed space. This specific worksheet helps to estimate TDI emissions when the volume of enclosed space (e.g.,mold or container) is known. For those processes that the weight of TDI used and the density of product are known, please refer to "M4a Enclosed Process-Weight." Potential emission occurs when the mold cavity, reactor or blend tanks is filled with the TDI isomers and when the reactor/blend tank is emptied into containers. The amount of emission can be calculated based on the volume of TDI filled into the mold cavity or the volume of container filled with TDI. The potential emission from enclosed process can be estimated from the following equation: Lenclosed-vol = Vair ? (1 / 359) ? (273.15 / T) ? (VPTDI / 760) ? MWTDI ? Cform Where: Lenclosed-vol = Emission from the enclosed process (lbs/year) Vair = Annual volume of released air (ft3/year), this volume is calculated by multiplying the volume in the enclosed space not occupied by TDI and the total number of them T = Temperature of the enclosed process (K) VPTDI= Vapor pressure of TDI at the operating temperature (mmHg) MWTDI = Molecular weight of TDI (174.2 lb/lb-mol) Cform = Proportion of TDI in the formulation. If only TDI is used then Cform is 1. This fraction is assumed to be constant and Raoult's Law applies. <?HHjN?H?NH?NHN%HgN?H?H?H?H?H?H?HHNc"N%S(N)R*N5a6NDaENGgIhLgTaUgXh[g\a]g_hdHeHlHmcyH?H?c?H?M?HVH?H?c?H?H?H?c?H?H?c?H=cAHHH?I?H?H?H?H?H?H?H?H?H?H?H?H?H?H?H?H?H?H?H????? ??4 ? ?p?? A* ??@???@tc0_cmd_m4b_showHideCalcDetails?H??]`? 1 6$Forms.CommandButton.1@ `???? ??4 ? ?l??AG ??@???<tc0_cmd_m4b_calc1_clearValues?v \?"1?]`? 1 6$Forms.CommandButton.1? L????? ?:7 ? ?N?? A ??@???CommandButton1? ??]`: 1 6$Forms.CommandButton.1? T???? ?r7 ? ?^?? 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J?6JmV ?mOo??Y????Y????˚?Q?+?J??Rd???? ?6?~???O*??_?????ۛf?ĉƝ?i???j>?IO?..ɱO?xٯL?/?u?0??XG0?M=QY?M{.?????H??΋??(?p??ۓ????󀶤?G.???p?a?Fk?y??0??4?|????PK-!??????[Content_Types].xmlPK-!1?_a?? ._rels/.relsPK-!???8 ?V)drs/shapexml.xmlPK-!???%?? drs/downrev.xmlPK?? ?]???] `<????<?Calculating Emissions from Enclosed Process with known volume The engineering calculation used to estimate TDI emission from enclosed process corresponds to the total volume of air released from the enclosed space at the operating temperature. This method assumes the worst case scenario that the volume of air released is saturated with TDI/TDI prepolymer vapor. Volume of air released is defined as the volume which is not occupied by TDI/TDI prepolymer in the enclosed space. Due to the relative size of the enclosed space and the low saturated vapor pressure of TDI, this assumption is considered reasonable. This specific worksheet helps to estimate TDI/TDI prepolymer emissions when the volume of mold or container is known. For those processes that the weight of TDI/TDI prepolymer used and the density of foam product are known, please refer to "M4a Enclosed Process-Weight". Potential emission occurs when the mold cavity, reactor or blend tank is filled with the TDI/TDI prepolymer mixture and when the reactor/blend tank is emptied into containers. The amount of emission can be calculated based on the volume of TDI/TDI prepolymer filled into the mold cavity or the volume of container filled with the TDI/TDI prepolymer mixture. The potential emission from enclosed process can be estimated from the following equation: Lenclosed-vol = Vair * (1 / 359) * (273.15 / T) * (VPTDI / 760) * Mw * KTDI * Cform Where: Lenclosed-vol = the emissions from the enclosed process (lbs/year) Vair = the annual volume of released air (ft3/year), this volume is calculated by multiplying the volume in the enclosed space not occupied by TDI/TDI prepolymer and the total number of them T = the temperature of the enclosed process (K) VPTDI= the vapor pressure of TDI at the operating temperature (mmHg) Mw = the molecular weight of TDI KTDI = the adjustment factor equivalent to the MDI molar concentration in the TDI/TDI prepolymer feedstock. Note: TDI monomer weight percentage can be used when it is close to molar fraction (unitless) Cform = the proportion of TDI/TDI prepolymer in the formulation. If only TDI/TDI prepolymer is used then Cform is 1. <??>A?A???A*?@A?A?Af??????AAAV?sAuAvA?A?A?A?A?A?A9A:?;FH?KEN?meofre}f~e?f?e?f?A?A?A?F?A?A?F?AGAhAzA?A?A?F?A?AAFA/A0F3A:A?A?A?F?AA%ABATAcFgAnAoApAqArAsAtAuAvAwAxAyAzA{A|A}A~AA?>?@U?????? ??????{+{???h???y??????K? To A1 Overview'A1 Overview'!B9??????? Percentage Required=You must enter a valid percentage (value between 0 and 100). 9d ????wwkk__SSGG;;//##?? invalid unitsvalid temp units are C, F, Ker#  ( &&22>>JJVVbbnnzz??????lInvalid EntryValue must be non-negative ??$%01<=HITU`almxy???s ry# Va $$00<<HHTT``llxx?????+ ry#Va??lError&The minimum temperature is set to 0 F. &&22>>JJVVbbnnzz????? Sheet11gg????D ZO?? )?? ߜ *?  d????MbP?_*+??%?????&ffffff??'ffffff??(??)??M?Nuance PDF?odXXLetterPRIV??"dXX333333??333333???&?<3?c#?U} }  } ?}  } ?8}   } )????????? ? ? ? ????????????????????? O"??D?l  ?!?"?@#?@$%J&?'?(?? #"?? $?? $?? $?? $?? %#Yk%?U???k???UD&? D'? B% Please enter values belowD&?dAD'?B? %?=? %?Z? &?[~ &$??? &??? &?!? '#\~ '$@? '?@? 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D? i?rT??0&?9 O??C&D?PE?t?H???????Ui??|??Əh uF,K?? ?jV? ?G|????j2p???IQ?z ?0b??Q??s |ܩ???A?珞???0C?? ???*?????-e??3?Qy?D??^?6?????`.?I5ߟ,??4??mu#?!/Xp????J`,?urj?\?HȘt[??Tf?f7?U?f??:c?F۠d?L?N??3?̫l?oWB??&2w???`C???]?n,@9?o$?s????gҰ??.* ΰ?V?U??.?+=??X.?5???P???(Vg???騫???j=?J??޽?!????RAQd???d#???z$Cu??,?ښfmE?m??????4?c??8??O???P|???:M?A???,L??QU-?ؤQٲ?j?u??? ?uԷ\?l?`???1}??u'ZQwB;VD߇?cA?????T?P????ퟯ@*ʹ????J? ?#?T??͂8?\&??K!DNzj??1?-?z?????.??????w????A?z%???UAM?Y??:E֪?????9??D????.?7? ??U?DiJ͚9?bʈ?l???/?~q?N??{N?g??????Y???_8??/Ѓ????m*??Fu????wl??LKPɚ)': ?//???????Yӻ?r??w??wvh&v??hPϹ? u????A(????7??!?2??o?ȡ$CN????Jx>????-#????SaF???.!,4d?~?9?+?v添n?? ???̒???{=?TpAp??{S????F???j??TC_Yۤm? ?????????b?=?GB41l??z?*?nK!?C?@??j[??8?f????(?R?TbK?ږ????r@?? ?As%? ;??(V???ܟ^????ax?J|[????|???p??B?? ?K??%?ϊK???????=????-??H?|??*??|e?c>%,O?N???PX?? ????&?U?#a?w??}??P????`?iZ?:?rL??.8?;(v??.8???38 ?2?H ?22钕sHV??bZ?:????<Ⱦ???=߭@??>phwK?ւ?+??C?;??[%?!?6??? *?a??E,??w"??? ??H?]?ɽLkY???˗?4???r??n???AC|??GU?? m?3???g?^N?]^???a??ߦU?C?bfU?????????&w???}є?q???{Yo?a??רGjE???G1?8ʷ?i!'?O??O?J?????????'?`??*??a?;??6??|?u?E??Ś?z??o??m??m?v????¨%?????qa(K?\??B;ْ?A???[?l???qFt|?3QA*?????"j:?̈0?????pFt|?? ???㜉?8???/???D?uoLz? v?L ?3Wˢ?r$?=\?nJE?ȴ{5? di?@??ף6]]?9l?C i?M???H??O??v??dC???Z+?D?\??2??^# ?qU?F+??(,,?73>-?A??~??C??r?s?R?WBr;ҭP?Vj#?C4[Z~?p?P??&T?ZaC?[?V"߭%?M*??I? ?e&o?]????]??q?s?z?dA?~??t qH?~ܘ?Xq?a??p-.?9N?D?6??4Z?  ?n-?gYZ???3??g????o??? ?lA?O??^?#\~s???PK-!??????[Content_Types].xmlPK-!1?_a?? ._rels/.relsPK-!8??/-?)drs/shapexml.xmlPK-!wE?9??drs/downrev.xmlPK???  3?] `???? <E  The open process moduled can be used to estimate TDI emission for applications where TDI containing products are cured with a significant fraction exposed to the atmosphere. Examples of open process applications are: Slabstock/Bunstock Carpet rebond foam Bonded foam production One important factor to consider is that in most cases, TDI reacts with other chemicals in the formulation such as polyol. It is important to inlcude a reaction rate of such reactions so that TDI emissions are not overestimated. The reaction of TDI is rather complicated and depends on many factor such as temperature, catalyst and the chemicals with which TDI reacts. A first order reaction rate is a starting point to estimate how much TDI is reacted away along the manufacturing process. The accumulated TDI emissions can be calculated by integrating the decay emission rate over the curing time period. See details in "M5a Open Process". This worksheet helps the user estimate this first order reaction rate. If you do not have the required information needed for this worksheet, go to "M5a Open Process" directly and the default 1st order reaction rate is provided. k_r=-(lna (R2 /100))/?t Where: kr = First order reaction rate (1/hr) R' = The remaining amount of non reacted TDI after certain given time (%), e.g., gel time or curing time ?t = The amount of time from TDI starts to react to the time when the remaining non reacted TDI reaches R' (%). < HH?H?H?HHHH?P?H?H?H?H?J?J?J?J?J?J?J?J?J?J?H?H?I?J?i?H?H?H1J2J3H?H?????? ?5???00= E_s/k_r ?(1 - e^(-k_r t)) Where: E_s=(0MW0_TDI?K_TDI?A?P_TDI?3600?Cform)/(R?T) (g/hr), Refer to worksheet "M8 Spill" for details on each parameter; for surface area A, please estimate the annual total surface area of the TDI containing product expo??????????????????????????????????????????????????????????????????????????????????????????????????<?????????????????????????????????B ??C ?(????Group 6"???$E )?]  `????? ?? ? ??G^???8]??8c?????H? Right Arrow 4???y??????K? 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"?ΰY\?Y?g???Y3ak?t?!?W?5dkH??%ZC?v?????? 6?.S?????+?ZŲq΢???2c8??VV??znU??V5e\???)?$g>^ݵ????Z>Ϩ?K?aC?:???2Z]???h????ۭ?yW?Rn;s?q??Է??}??n?????d?jc??4?MY?e??R}????FEa?H?=?????W3x?'??#+??pa?,??j?n??^4?????|??g??OG'v/:MZ?̬?P? ,??0N???5NGY?[:???h?Bٴ?5??8%?)Y\x??? ??bcD ^}|؛kla??????Ed????^??C??#?/???|3?_?r?E?1i?W???b??F*?XH)?ϕ????G?*o?UV?8\s!W???,[?d5???d ȥL?9?qfي’????3A*2a?D?e???0?g0??T?ؙ?2???L,S???J?&?$????P?d???ժ????B?a*7w?YD7??|??ޯ6:]&?_?װ?$"?|???7p?St????????5?3?????1a?K??$ۆ???b?n??? 7?NJ?.??im?WYW????҉t;{??6u?\???*?dS??- ??b??G?\8n?ژNP??^L L?\?&?????y|Γ?Qh?v?;?e??EW??/?=>???I:l???cL?Bgz~Y)0?>??a??r?&?Wmg(?+=??O??!????̇??`?r?????????Y?&Ҫ?Y%`?? m?Q??W?J??嗺?*????? ?}2????PK!ȁ?V"?drs/downrev.xml\?_O?0??M??5?M??O6)???&8?k?Z????-l??#?o=??wnO??FWd'?/??ui2??f?!??ߍ?? L.*k$???0?\_?E???,?n?C?O?"?MB?? ???؍48S?iP?5͝?1\W??ؐjQ?P??|,d???j?TQ????2ճ??/?*?????= ? gs`oJ??Ǫ?u2?^r1???ve?>H??жŦ0? M53Ya]{V?j?l͡$??ы?])/Q?????j? hK?Ǟ`\} ???p??yH?ˇ?8????PK-!??????[Content_Types].xmlPK-!1?_a?? ._rels/.relsPK-!@4??6:?)drs/shapexml.xmlPK-!ȁ?V"??drs/downrev.xmlPK???@? !??] `<??"i?<? Guidance: The open process module can be used to estimate TDI/TDI prepolymer emission for applications where TDI containing products are cured with a significant fraction exposed to the atmosphere. Examples of open process applications are: Slabstock/Bunstock Laminate boardstock Metal skin panels Carpet backing/flooring/coating Belt and Tire Cord Bonded foam production Adhesives/sealants Oriented Strand Board (OSB) Spandex One important factor to consider is that in most cases, TDI/TDI prepolymer reacts with other chemicals in the formulation such as polyol. It is important to inlcude a reaction rate of such reaction so TDI/TDI prepolymer emissions are not overestimated. The reaction of TDI is rather complicated and depends on many factors such as temperature, catalyst and the chemicals with which TDI reacts. A first order reaction rate is a starting point to estimate how much TDI/TDI prepolymer is reacted away. The accumulated TDI/TDI prepolymer emissions can be calculated by integrating the steady state emission at a short period. Please see details in "M5a Open Process". This worksheet helps the user estimate this first order reaction rate. If you do not have the required information needed for this worksheet, go to "M5a Open Process" directly and the default 1st order reaction rate is provided. k_r=-(lna (R2 /100))/?t Where: kr = First order reaction rate (1/hr) R' = The remaining amount of non-reacted TDI/TDI prepolymer when the product is considered as "Cured Product" (%) ?t = The amount of time from TDI/TDI prepolymer is mixed with the rest of the formulation until the product is considered as cured. <?N H H?HHH,HLH_HvH?H?H?H?H?H?H8PwP?P?H}H?H?H?HGHHH-H.J/J0J3J4J:J;J?JAJBJCHDHKOLJMiNH\HrH?H?H?J?J?HHHhHi>?@U?????j???y??????K? To: A1 Overview'A1 Overview'!B9??????_  Curing Time*Curing Time must be positive, please retryAOd''?? % of unreacted MDI/pMDIM% of unreacted MDI/pMDI must be higher than 0 but less than100, please retry ?H?????z> 6?????X@&&? 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Please refer to "M7 Spill" for details on this method. In order to account the reactivity of TDI/TDI prepolymer when mixed with polyol in many applications, one modification is made to the EPA method. When TDI/TDI prepolymer is mixed with polyol to produce the final product and during the following curing process, TDI/TDI prepolymer is reacting with polyol and therefore the available TDI monomer to be released into the atmosphere is reduced. An estimated first order reaction rate (kr) is introduced to account this reactivity. kr is affected by many factors such as the type of polyol, TDI/TDI prepolymer mixture and catalyst. kr is calculated in the range of 10-3/s according to "Catalysis in Aliphatic Isocyanate-Alcohol Reactions" conducted by Bayer Corporation. If you have calculated kr from "M5 Open Process" main page, please enter the value of kr instead. Table I and II in this study are used to estimate TDI reaction rate with different catalysts. If the users have their own reaction rate, please change the default value to their own values. The total TDI emission from open process can be estimated by the equation below: Etotal = +"_0^t?%00(E0_s?e^(-k_r t))dt0 = E_s/k_r ?(1 - e^(-k_r t)) Where: E_s=(M_x?K_x?A?P_x?C_TDI)/(R?T) (g/hr), please refer to worksheet "M7 Spill" for details;, for A, please estimate the annual total surface area of the TDI/TDI prepolymer containing product exposed to the atmosphere. kr = First order reaction rate (1/hr), default value is 7.2/hr; t = The amount of time starting from the mixing of TDI/TDI prepolymer with polyol and ending when the product is considered fully cured (hr). 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D{? <? @??4? ???3?( ? ????? ?? ? ?\???D^?0e?0e????????????TextBox 1"?)??#PK!??????[Content_Types].xml???J?0????*m?i??G]`H?m?6 ?Xw??t?.? g???#?W?i3E??)?.+?7?? >?O?N? ?ޑ?1??ˋz? ?"?+R ?R?hB.} ?/???????0???x??M ??e??`??|X}?????đ ?I`߽??N4a?G2?$?R?KI?Z?)?4?(?M?9`?ctB{????m?:?f@?`??3??n?|O?????,ܗ?r???޾?j??x??R0T ?,?0????@?????}W?B?L??Ǭ5v??PK!??z dJdrs/shapexml.xml?\?r۸??L??+g??d?N4?w?κ??8I?d?"! pP?????G???A(?v-ɲ,???H?? ??|?*6?I?;Q?R??бI??w?o_/^????\'\-:?X???ӿ???ub?\?c?Ю??N4?>kW?.????Ʉ?Ӟ?)????jb????ڨՎ?.??'n ?_M`we?A?]? ?ܛ?uϦ??Dؙ^??F?m???1`:????#???A!)?5H ??ѥ???h? ?y?@???u???l ??:?????G?N?)_??ɅT?!??P?+ˆ\u?n?8?Og?)??t.6?Do[?V!Y屝?wg????&R?eJ???ͬo???Un?_???C?j??J_eq?,??B??3?Mz$??O ????0?`TQ'_???A??t"?_??ǡ???.?I???H? ?C??;,?6W? ݸ0?h+\?{???^j?Ǚ??#?s%?VF#v7??s$ }??@}x??A?%?.??o?~?|A"?K$???@;z??`f??~H?F?~?s??c5d?A?9C??`?@???_ R???_O??B?ma̳???fZH??4=?o?3 vaY?Sɘwa?ac?[x ??/ܳ??{6ࠐ?&?X?=?aX??+??^???퓘?U?; ?????@?^^?p?0?KFcC??#?[?r?????l?t"4???i?涾?_?KV??J?"?qm??F??q????&?J.x*°#4?n?h?[???2mh?D??? ?r?cYծ-??R??Ȇ??f??X?b ?R(?v??E.??ƒ?{Jr?j??ȧS&Jf?O?@|B\"?;??ܺ??F???0o?#l??;齪~`gz[tɝ?S??i?\??}n)ښ?U??????P??zXa??c?Y g?b??.???.??k?fJ?FI?Fp?w?G?OÌp?? ? ?_??a?F ?Ke?HБe P??I??`?*???qm?"Aq???ov?x??Q ??h?Fpw?%??8`?Mt`7?F??x?.?y?-??? d?f>?![??M????V?Ku???[V(~?/?!??\ٟ?~ -? ?jV????9????M x5?d?h???;Z????W ?WԐ?????? ??wqL?k{?oV 7o/]Rq?z??,??)?o;9???PK!K??p?drs/downrev.xmlt?OO1??&~?fL???fE ِ(r1?z?V??ٶk[a??kz?6o?~o?:???&[?|e??^Daee ?/?)????F1?+???و?ݙ?ڮBA0??!gP?? )??T???m????:?JWP???uM?(J??? %oԴTb??? ?S?v?$b3?.?A????&?]^??=???p2????|??]ܓd?g???????m?)??B[gF????YM??1H?[w^??y?U?n?*??n#?2ؿ??rI?&??}??;????PK-!??????[Content_Types].xmlPK-!1?_a?? ._rels/.relsPK-!??z dJ)drs/shapexml.xmlPK-!K??p?? drs/downrev.xmlPK?????]`???8?<9 This worksheet serves as an alternative approach when neither of the following is applicable to your process or you do not have enough data to use them: M4: Enclosed Process M5: Open Process This worksheet assumes the manufacturing process using TDI is enclosed by a control measure. For example, when producing slabstock foam, the entire production line is enclosed by a ventilated tunnel. Note the difference between such enclosure (control) vs. the enclosure of a mold/cavity. Use "M4 Enclosed Process" for the latter case. Also the exhaust air in this module specifically refers to the control measure which the emission is considered as stack emission. Do not confuse with "M2 Fugitive Monitoring Data" which the exhaust air from the general building ventilation system. If you do not have measured TDI concentration in exhaust air, module M6S assumes the worst case scenario that all exhaust air is saturated with TDI vapor. This assumption will siginificantly overestimate your reportable emission in most cases. Do not use M6S if you can use M4, M5 or M6. The emission can be calculated when the measured airborne concentration in the exhaust air is available: Lexh.air = Ctdi/1,000,000 * (Qec / 359) * 60 * (273.15 / Tamb) * MWTDI * to Where: Lexh.air = TDI emissions in the exhaust air (lb/year) Ctdi = Average TDI concentration in the exhaust air (ppmv) Qec = Air flow rate of exhaust fan of the emission control measure (ft3/min or CFM) Tamb = Ambient temperature (K) MWTDI = Molecular weight of TDI (174.2 g/mol) to = Total number of working hours per year (hr/yr) <??A)A?A?A?A?A?AA?C ACA,A-A?C???E???E???E???E???E?????E?????A?A?A?F?A&A'F*AaAbFdA?G?A?A?F?A?A?F?A?EA5A6A7A8???? ?? s ?V?A) ??@???,cmd_calc6_clearValues?!?["??]` 1 6$Forms.CommandButton.1<L???? ?? s ?X?A' ??@???.cmd_calc6_showHideCalc?? ?]` 1 6$Forms.CommandButton.1?`???? ?? s ?X?AV ??@???.cmd_Number_Sets_Select????!/?]` 1 6$Forms.CommandButton.1?H???? ?? s ?Z?A( ??@???0cmd_calc6_showHideGuide??S?]` 1 6$Forms.CommandButton.10T?????? ?5???00??B ??C ?(????Group 7"??~??"v?] `????? ?? ? ??G^???8]??8c?????H? 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For example, when producing slabstock foam, the entire production line is enclosed by a ventilated tunnel. Please note the difference between such enclosure (control) vs. the enclosure of a mold/cavity. Use "M4 Enclosed Process" for the latter case. If you do not have measured TDI concentration in exhaust air, Module M6S assumes the worst case scenario that all exhaust air is saturated with TDI vapor. This assumption will significantly overestimate your reportable emission in most cases. Do not use M6S if you can use M4, M5 or M6. 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M?9?5?-??Nm?:??k??J?{aF??-??Uq??Oɖ?*????k'?J???????-e+pS?G}g???G?Ap??%??c*C?l??w?R?uءPTr??Б!E?H????vqh?6?I?}ƺ???Dٚ*G -?=????JP|%??Q?5R???'?1y?????Ẅ??n?>\b???]]???b????????????????!Oj?=?/??k?"4???Hvc,.????MШj???Lv??~???+??? ?kjl?!.?*ڴWwo=?f???Po1 ???S?|?^!?????H??U????????y?]7?1?[;?? ??i??f?1???????+^???_g?Nz?:?Uv???x????=?]????:???;?;?uL???????????U??i?:?_???ι?۽}٧??:??~???LM????6??vq?y?@?????J8/- ?q?S?Дs????ߙ5?XSsILy?E??eNzC??#??? ????? ?u`??e?Q/8?{A?/!MO???x??/??PK-!??????[Content_Types].xmlPK-!1?_a?? ._rels/.relsPK-!?X?*Q)drs/shapexml.xmlPK-!?#{?%?? drs/downrev.xmlPK?: ?C?w??]`<????<?Calculating Emissions from Exhaust Air- Saturated The engineering calculation used to estimate TDI emission from exhaust air with saturated TDI/TDI prepolymer corresponds to the total volume of air released through exhaust fan. This method assumes the worst case scenario that the volume of air released is saturated with TDI/TDI prepolymer vapor. Volume of air released is determined by exhaust fan speed Potential emission occurs when the mold cavity, reactor or blend tank is filled with the TDI/TDI prepolymer mixture and when the reactor/blend tank is emptied into containers. The amount of emission can be calculated based on the volume of TDI/TDI prepolymer filled into the mold cavity or the volume of container filled with the TDI/TDI prepolymer mixture. The potential emission from exhaust air with saturated TDI/TDI prepolymer can be estimated from the following equation: Lexh.satl = Vair * (1 / 359) * (273.15 / T) * (VPTDI / 760) * Mw * KTDI * Cform Where: Lexh.satl = the emissions from exhaust air by monitoring (lbs/year) Vair = the annual volume of released air (ft3/year), this volume is calculated by multiplying the volume in the enclosed space not occupied by TDI/TDI prepolymer and the total number of them T = the temperature of the enclosed process (K) VPTDI= the vapor pressure of TDI at the operating temperature (mmHg) Mw = the molecular weight of TDI KTDI = the adjustment factor equivalent to the TDI molar concentration in the TDI/TDI prepolymer feedstock. Note: TDI monomer weight percentage can be used when it is close to molar fraction (unitless) Cform = the proportion of TDI/TDI prepolymer in the formulation. 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Such accidental releases must be reported under section 313. the EPA Emission Inventory Improvement Program (EIIP), Chapter 16, section 3.7 lays out a basic model to calculate the liquid evaporation rate based on a method proposed by Crowl and Louvar in 2002. This method requires to estimate the mass transfer coefficient of chemicals. EIIP suggests using water as the reference . However, mass transfer coefficient developed based on water may only be applicable for high volatile chemicals, due to the low vapor pressure of TDI, this method has higher emission rate estimate than the method discussed below: In EPA EIIP, volume II: Chapter 8, Methods for Estimating Air Emissions from Paint, Ink, and Other Coating Manufacturing Facilities (EPA, Feb, 2005), a method is used to estimate evaporative losses from open processes. This method is compared with other methods and selected to estimate TDI emissions from spill. A few factors determine the emission rate: 1. The vapor pressure of the material 2. The size of the spill 3. The temperature of the surrounding area 4. The air velocity above the surface 5. The time that the liquid from the spill is allowed to evaporate 6. TDI isomers % in the liquid mixture E_x=(M_x?K_x?A?P_x?3600?KTDI)/(R?T) Where E_x = Evaporation rate (g/hr) M_x = Molecular weight of TDI monomer = 174.2 (g/mole) K_x= Gas phase mass transfer coefficient for TDI (m/sec) A = Surface area of liquid pool (m2) P_x = Vapor pressure of TDI at temperaure T (Pa) R = Ideal gas constant (8.3144 Pa ? m3 ? K-1 ? mole-1) T = Temperature (K) KMDI = Average percent of TDI isomer in the mixture The gas phase mass transfer coefficient K_x (m/s) can be calculated as equation 8.4-20 in the EIIP, volume II: Chapter 8 (USEPA, Feb, 2005): K_x=(0.00438?U^0.78?0(D_x/3.1?10^4)0^(2/3))/3.28 Where U = Air velocity above the surface (miles/hr) D_x= TDI isomer diffusion coefficient in air at temperature T (ft2/s) The TDI isomer diffusion coefficient in air at temperature T can be calculated as : D_x=(0.01013?T^1.75?0(1/M_x +1/29)0^0.5)/(P?0[("1?%0?_x)0^(1/3) +(020.1)0^(1/3)]0^2 ) Where T = Temperature (K) D_x= TDI isomer diffusion coefficient in air at temperature T (m2/s) P = Atmosphere pressure = 101325 Pa ?_x = Group contribution values for TDI summed over atoms, groups and structural features given in Perry's Chemical Engineers Hanbook (8th edition, 2008). ?_x for TDI monomer is 160 and for air is 20.1. Please note: when TDI spills occur, TDI is very likely to react with moisture in the air and with any polyurethane formed during the reaction. However, the reaction rate can be affected by many factors such as the moisture content and temperature. This worksheet does not consider any reaction occurs during the spill period and therefore gives the worst case estimate. When hydroxyl group is not abundant and there is no catalyst in the system, such assumption is considered reasonable. The relative reactivity of NCO group with several active hydrogen-containing compounds can be found in Table 1.3 in "Vilar, W, Chemistry and Technology of Polyurethanes, 2002." 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Such accidental releases must be reported under section 313. the USEPA Emission Inventory Improvement Program (EIIP), Chapter 16, section 3.7 lays out a basic model to calculate the liquid evaporation rate based on a method proposed by Crowl and Louvar in 2002. This method requires estimating the mass transfer coefficient of chemicals. EIPP suggested using water as the reference. However, mass transfer coefficient developed based on water may only be applicable for high volatile chemicals, due to the low vapor pressure of TDI, this method has higher emission rate estimate than the method discussed below: In the USEPA EIIP, volume II: Chapter 8, Methods for Estimating Air Emissions from Paint, Ink, and Other Coating Manufacturing Facilities (USEPA, Feb, 2005), a method is used to estimate evaporative losses from open processes. This method is compared with other method and selected to estimate TDI emissions from spill. A few factors determine the emission rate: 1. The vapor pressure of the material 2. The size of the spill 3. The temperature of the surrounding area 4. The air velocity above the surface 5. The time that the liquid from the spill is allowed to evaporate 6. TDI monomer % in the liquid mixture E_x=(M_x?K_x?A?P_x?3600?C_TDI)/(R?T) Where E_x = evaporation rate (g/hr) M_x = molecular weight of TDI monomer K_x= gas phase mass transfer coefficient for TDI (m/sec) A = surface area of liquid pool (m2) V = air speed (m/sec) P_x = vapor pressure of TDI at temperaure T (Pa) R = ideal gas constant (8.3144 Pa ? m3 ? K-1 ? mole-1) T = temperature (K) CTDI = the average percent of TDI monomer in the mixture The gas phase mass transfer coefficient K_x can be calculated as equation 8.4-20 in the EIIP, volume II: Chapter 8 (USEPA, Feb, 2005): K_x=(0.00438?U^0.78?0(D_x/3.1?10^4)0^(2/3))/3.208 Where U = Air velocity above the surface (miles/hr) D_x= TDI monomer diffusion coefficient in air at temperature T (ft2/s) The TDI monomer diffusion coefficient in air at temperature T can be calculated as: D_x=(0.01013?T^1.75?0(1/M_x +1/29)0^0.5)/(P?0[("1?%0?_x)0^(1/3) +020.10^(1/3)]0^2 ) Where D_x= TDI monomer diffusion coefficient in air at temperature T (m2/s) P = Atmosphere pressure = 101325 Pa ?_x = Group contribution values for TDI summed over atoms, groups and structural features given in Perry's Chemical Engineers Hanbook (8th edition, 2008). ?_x for TDI monomer is 140 and for air is 20.1. Please note: when TDI spills occur, TDI is very likely to react with moisture in the air and any polyurethane formed. 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According the USEPA Emission Inventory Improvement Program (EIIP), Volume II: Chapter 7, Preferred and Alternative Methods for Estimating Air Emissions from Surface Coating Operations, emissions from spray coating operations in spray booths may be calculated by the equation below. This approach is also accepted by state EPAs. One simple illustration is given by the Office of Compliance Assistance and Pollution Prevention, OH EPA in "Fact Sheet: Calculating Emissions from Coating and Painting Operations". Lsp = Weight of TDI sprayed * (1- Spray Gun Transfer Efficiency) * (1- Spray Booth Filter Efficiency) Where: Lsp = the particle phase emissions in lb/year for spray coating operations. 2. Step two: Calculate the vapor phase TDI/TDI prepolymer emission during drying or curing process. After the part is sprayed with TDI/TDI prepolymer I containing coating, it may be dried in an oven or just let air dry. If the part is dried in an oven, the emission can be modeled as an enclosed space. It assumes the volume of the oven is saturated with TDI vapor. If the part is let air dry, the emission can be modeled as open process. The difference between the emissions from air dry vs. open process is the time. For air dry, only emissions during the time of air drying should be counted. When the air dry occurs indoor, please note to take account the exhaust air filter efficiency. 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To A1 Overview'A1 Overview'!B9????? ?? Percentage Required=You must enter a valid percentage (value between 0 and 100). 9?d 68NPfh~????????????? invalid unitsvalid temp units are C, F, Ker#  ( 33??KKcc{{????????  ?s ts#va 11??IIaayy????????  ?6lInvalid EntryValue must be non-negativeay==11????????UU????mmII??aa??yy????..????????FF^^vv????  ?+ ry#Va**?? Invalid EntryxValue must be between 0 and 24, since when the coating material is mixed, it is expected to be sprayed within 24 hours. I //GG__ww???????????? Invalid EntryJValue must be between 0 and 720. The max curing time is set to be 30 days. iec8" 00HH``xx????????????L 1st Order Reaction Rate RequiredKYou must enter a valid first order reaction rate (value must be positive).  99QQii??????????????lOut of Temperature Range&The minimum temperature is set to 0 F.erti 33KKcc{{??????????  ? Sheet28gg????D ZO?? 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[H?BG??-Z?????Hu?[?? ??C_ sAT$?rq?f??y?Sc?}?1?e??\???nܶO_???????hn?@??)? ??E?`??ujk???E\&???͗?;F?;?3J????$i???S?V?f?;?P̉l?33?P?R)3?Ȳ.L??3 ?b,Լϗ??TJ?g?ϟ??tJ~???Wr?x?yBXm??E??YiI?o??ug??v?l?883??Os???u??k?????????~???????EϏ??_n?ܩ?ʙ>?_&.????f`??????㞓#???i?-H???????Y???7?9oO?31<ל+??t??|???朖?h????v?w??%?w??YN?|}_8???o]f??-+????}[?Q5Ƶ??oE????[??G#?p?Zg?OqRht??o??{R?C???/????7t??U?4M???K?~??? dr??h???4N?ɗ?tpAN????v?????Z?xK?[??:?>m+O??5Lwb[??pv?(????/9?7?sQ??o;&Ӱ~6???B}??hw?"?#_?N>N?? c?q?Z???"[?l??n?????r???)?L?,g?\ K?2p?ܣ[?1#???XY?;????k?%K­0?i?O???%?{?9?c U??\??? ??&?ߒM????*?(2?^1˜޸??7???|?????PK!Xi??&?drs/downrev.xmlL?AO1??&??fL?I??l)????`b?նˮn۵???{P??7?y?S????t?C?b@??N?v??m1????JT?j[`8??苞r;??y\bCOp(b?{?Yh#B???b/wވ?ү??b??MES?2jDiqC!j=.?????k^?|?>?X5?O???sӍ???ft$?&??"]?٧?.?ſa?n?8?????T3??0"ư0?M5??p~?ν3Ļ????^?/ytD??: qlK?ր???p?????֔eh=??I?hz~ ???~??PK-!??????[Content_Types].xmlPK-!1?_a?? ._rels/.relsPK-!6m?Y? ))drs/shapexml.xmlPK-!Xi??&??drs/downrev.xmlPK?? ??????]l`???/?<_TDI Vapor Pressure/Temperature Chart TDI Vapor Pressure Chart is a table that lists the Vapor Pressure of 2,42 -TDI vapor pressure (VP) at temperature from -10 oC to 200 oC. To determine the vapor pressure of 2,42 -TDI and 2,62 -TDI at a temperature not listed or if the temperature range is outside the range of values listed, you may use the following equation: Log (TDI VP in Pa) = 9.66 - 2120 / (Temperature in ?C + 203) Where: Temp in K = 273 + Temp in oC Temp in oC = 5/9 x (temp in oF  32) Note VP (mm Hg) = 0.0075 * VP (Pa) <?~$%?&???????????????k?l??????????????????????? ? ?.?/? ? ? ?m? ? ?f??XD^????(k??????????Text Box 35"?d ??^ PK!??????[Content_Types].xml???J?0????*m?i??G]`H?m?6 ?Xw??t?.? g???#?W?i3E??)?.+?7?? >?O?N? ?ޑ?1??ˋz? ?"?+R ?R?hB.} ?/???????0???x??M ??e??`??|X}?????đ ?I`߽??N4a?G2?$?R?KI?Z?)?4?(?M?9`?ctB{????m?:?f@?`??3??n?|O?????,ܗ?r???޾?j??x??R0T ?,?0????@?????}W?B?L??Ǭ5v??PK!????5drs/shapexml.xml?W?n7}/????5??????"@.F??]M/????@?O/ ?l?h+e&????z??=A0!?ƍQ?z?`?????ݔf?~`K{z)??*?Q???L)??ԃL(???-Zˢ? ?4?&݄;?????ݦ?dP?y?km>??w??Ȩ-?M?J?CӅ??0??$????9???????Z?P????f????????d??䁢ct8?G/O?y?U????;??k Forms.ComboBox.1?d #>? @????? ?j???y??????K? 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H!L'( ( P?ErrorA@N?D?o????P]??? ~.z???m1_calc2_vt_input z%^(>?2? m1_calc2_lt z%^(>? ?m1_calc2_tr_input z%^(>?4@?m1_calc2_tamb_input z%^(>?Expected value: 2.50E-06?m1_calc2_Result z%^(>o?????]??? ~.z??C46, C47, C54 z%^(>?gal/year?D46 z%^(>?D?C50 z%^(>?F?D50 z%^(>?&ws.Range("m1_calc1_result").Value = ""o????]?P? ~.z??m1_calc2_vt_input z%^(>?gal?m1_calc2_vt_input_units z%^(>?? m1_calc2_lt z%^(>??m1_calc2_tr_input z%^(>?F?m1_calc2_tr_input_units z%^(>?D?m1_calc2_tamb_input z%^(>?F?m1_calc2_tamb_input_units z%^(>?&ws.Range("m1_calc2_Result").Value = ""o????p?&?]????????? 'V?BstrMsg = "Selected worksheet: " & Me.Combo_worksheetLinkList.Value?3MsgBox strMsg, vbOKOnly, "Next Worksheet Selection"?'V 2 .B@0? 4(6? 4(8? ??!<!>$:(@ ??!<!>$:B@H?Sheets(Me.Name).Visible = False? 4(8? 4(6 2 .B@B?d'V?Dh|??`?&X? ?0Error. Combo_worksheetLinkList_Change. in sheet: ??!? . at step= V F?Err No.= H!J?.  H!L'( ( P?ErrorA@N?D?o?????&?]?P?h]?? ??????]??? 'V?A7'?? 4(8? 4(6? 'V?'??7:41?+??'V 2 ~B@0? ??? ?? ?$?$X!Z!\ ?$?$X!Z(\????Z'V ?$^B@H?d'V 2 ~B@B? 4(8? 4(6?D0|??(?& ? 4(6? 4(8??5Error. cmd_calc1_showHideCalculations_Click. at step= V F?Err no= H!J?.  H!L'( ( P?ErrorA@N?D`o??X? ??! ??!<(>o??0????(????$?Attribute VB_Name = "She@et5" ?Bast0{000?20820- C$0046}|Global!?Spac?False dCreatablPre declaId?TruBExposeTemplateDeriv$?Bustom izD2Control??Comb?o_works??LinkList, 3572, 0, MSForms, Box???&mandButton1, 2?649,  "??$cmd_calc1_showHPideC?u?~i?onF28/K''?learAllCp, 97?;??%2\_cD??%4?Opt@0 ?ylic?it P@sA@u Sub ?=ckValues_C k() Dim ws 0As W?lSe?t= Act?B?CCws.Ra?nge("m1DVqm_input").???133690^ _uni?ts?"ft3@sCA(tamb?2?? C?percentage_(mdi?5Wre(sul) " 3ec t?kv?/: 3.@35E-04?? End?4?6?U'8On Error GoTo er`r_sub?-;stepA;Integer, str(Ms?z ?6????? ??????c??????????????????????????x3Combo_worksheetLinkList, 3572, 0, MSForms, ComboBox/CommandButton1, 2649, 1, MSForms, CommandButton>cmd_calc1_showHideCalculations, 281, 2, MSForms, CommandButton1cmd_clearAll_calc1, 97, 3, MSForms, CommandButton1cmd_calc2_clearAll, 91, 4, MSForms, CommandButton??ME??????????????????????????????????????????? ????????????????????????????????????????????????????????????????????????????????????????????????PSL????S????S?????(? ?????h? ????"?p?x??????? ??????? ?? ?? ?? ????????? ?  ?@?X?p????????? ????? ???????????2?8? ????? ?????@?H? ?????X?`? p? ?? ??????????? ?? ??|??H?`? ?????h? ????"?p?x? ?? ?????(??"??(??0?>8? ????? ?????x? ????"????? ?? ?????$??"????? ????? ,0? ?????`? ????"?h?p? x? ?????(??2??"??(?08?*h?2?? ,?? ?????? ????"???? ?????8? H@? :?? ????????? ?? ?? ????? ? ? &0 ? ????? X ? h ?x ?? ? ????? ?????? ?? ?? ??? ?8 ?P ?X ? ????? ????"?` ?h ?p ?? ?? ? ?????? ? ? ? ? ? ? ? ?????? ?? ?? ? ????? ????? ????? ? ? ?28 ?p ? ????? ?????x ?? ? ?????? ?? ? ? ? ? ? ?????? ?? ?? ? ? ? ? ?| ?? ?? ?? ? ????"?? ?? ? ?????? ? ????????? ???x?]?@? ~.zX??: ?m1_calc1_qm_input z%^(>$X?ft3?m1_calc1_qm_input_units z%^(>??m1_calc1_tamb_input z%^(>?C?m1_calc1_tamb_input_units z%^(>?2?m1_calc1_percentage_mdi z%^(>?Expected value: 3.35E-04?m1_calc1_resgAS ?ngGrndxAry(10)?Var?ian?v?FMaxh?focu?I? ?b= 9M?r#??A70AppSa?Y.En遍Ev?/s?H???A?ScreenUdpd?ng??1??5e= 7?'!?)?"7:29 ?&2"45:7?k48:4?%ac51:5?X%3?? 55:56%?4"6???5?-m6?7?71?:7? ??D0e{?.Unprot?T8 (g@Ӏ???_phass@?dd?? ??@%1 ?Ma@A? ??Rows(?A* ?))@9tireE .??den?NHot _en N?ex??? ???I$;?C??J).Sel@??10?iPr>?)?)?p? ?)?)g? exit?:: ?E?C@ End?< Priva te9mandButton1_C?ok(TOn q@or CJ?Dim?7 As I?nteger,?#??String? rndxAry(10)?Vari?ant, ??1Max?foxcus???BX= 9CrC = "?A7?BI?????I Υ??1Ě?.= 1 ?!E=)??"7:4^1#?I?2?A?B???.Unpr??F@4?_ @>a?(?C ?MRows(?a0?))`stire .HiddeBn?Not _e?n Nexă??Ud9dR?d(?1)?.i???ui?} ?:?G??:?`????)? ?????cmd_c?alc1??ow@3?eC?ul?scs󟋉?no???e??)?A??;?ኁ(???Qĩ??H?lc1_tamb_input z%^(>?C?m2_calc1_tamb_input_units z%^(>?Expected value=1.43E+00?B45 z%^(>? ws.Calculate? 4(8o??x?`]??? ~.z? 4(8??m2_calc1_ctdi z%^(>?? m2_calc1_VB z%^(>?? m2_calc1_Nhr z%^(>?D?m2_calc1_tamb_input z%^(>?? m2_calc1_t_o z%^(>?F?m2_calc1_tamb_input_units z%^(>??C48 z%^(>?ppbv?D48 z%^(>??C49 z%^(>??C50 z%^(>??C51 z%^(>?D?C52 z%^(>?F?D52 z%^(>??C59 z%^(>?ppbv?D59 z%^(>??C60 z%^(>???C61 z%^(>??C62 z%^(>?D?C63 z%^(>?F?D63 z%^(>??C70 z%^(>?ppbv?D70 z%^(>? ? ? ? ? ? ? ? ? ? ? ? ? ? ? ? ? ? ? ???? ? ? ? ? ? ? ? ? ? ? ? ? ? ? ? ? ? ? ? ? ? ? ? ? ? ? ? ? ? ? ? ? ? ? ? ????? ? ? ? ? ? ? ? ? ? ? ? ? ? ? ? ????? ? ? ? ? ? ? ? ? ? ? ? ? ? ? ? ? ? ? ? ? ? ? ? ? ? ? ? ? ? ? ? ? ? ? ? ? ? ????? ? ? ? ? ?  ????? ? ? ? ? ? ??C71 z%^(>??C72 z%^(>??C73 z%^(>?D?C74 z%^(>?F?D74 z%^(>??C81 z%^(>?ppbv?D81 z%^(>??C82 z%^(>??C83 z%^(>??C84 z%^(>?D?C85 z%^(>?F?D85 z%^(>??C92 z%^(>?ppbv?D92 z%^(>??C93 z%^(>??C94 z%^(>??C95 z%^(>?D?C96 z%^(>?F?D96 z%^(>??C103 z%^(>?ppbv?D103 z%^(>??C104 z%^(>??C105 z%^(>??C106 z%^(>?D?C107 z%^(>?F?D107 z%^(>???C114 z%^(>?ppbv?D114 z%^(>??C115 z%^(>??C116 z%^(>??C117 z%^(>?D?C118 z%^(>?F?D118 z%^(>??C125 z%^(>?ppbv?D125 z%^(>??C126 z%^(>??C127 z%^(>??C128 z%^(>?D?C129 z%^(>?F?D129 z%^(>??C136 z%^(>?ppbv?D136 z%^(>??C137 z%^(>??C138 z%^(>??C139 z%^(>?D?C140 z%^(>?F?D140 z%^(>? ws.Range("B45").Value = ""?Application.EnableEvents = True?ws.Range("B45").Value = ""? 4(8o??????&?]??]?? ?0?h??]??]??]??? 'V?A7'?? 4(8? 4(6? 'V? '?? Application.EnableEvents = False? ~.z?m2_num_selection z%^!>'??rndxAry(1) = "7:31"?42:43?+??53:54?+??64:65?+??75:76?+??86:87?+??97:98?+??108:109?+??119:120?+??130:131? +??141:142? +??ARows("7:31").EntireRow.Hidden = Not Rows("7:31").EntireRow.Hidden?CRows("39:41").EntireRow.Hidden = Not Rows("39:41").EntireRow.Hidden?Application.EnableEvents = True?'V 2 ~B@0? ??? ???"+ 1 ?$?$X!Z!\ ?$?$X!Z(\????Z'V ?$^B@H?d'V 2 ~B@B? 4(8? 4(6? ?@????? ?F??]/??c??????????????????????????x3Combo_worksheetLinkList, 2150, 0, MSForms, ComboBox7cmd_calc1_showHideGuid, 1185, 1, MSForms, CommandButton7cmd_Number_Sets_Select, 1017, 2, MSForms, CommandButton6cmd_calc1_showHideCalc, 194, 3, MSForms, CommandButton5cmd_calc1_clearValues, 171, 4, MSForms, CommandButton??ME????????????????????????????????????????? ????????????????????????????????????????????????????????????????????????????????????????????????PSL????S????S????????? m2_calc1_VB z%^(>? N? m2_calc1_Nhr z%^(>??m2_ca?D0|??(?& ? 4(6? 4(8??-Error. cmd_calc1_showHideCalc_Click. at step= V F?Err no= H!J?.  H!L'( ( P?ErrorA@N?Dho??`???&P]?(?@?X?p?'V 2 .B@0? 4(6? 4(8?? ??!<!>$:(@ ??!<!>$:B@H?Sheets(Me.Name).Visible = False? 4(8? 4(6 2 .B@B?d'V?D`|??X?&P? ?0Error. Combo_worksheetLinkList_Change. in sheet: ??!? . at step= V F?Err No.= H!J?.  H!L'( ( P?ErrorA@N?D?o??????&?]????]?? ???0?H]?`? 'V?C6'?? 4(8? 4(6? 'V?'??7:31?+??rndxAry(2) = "42:47"?rndxAry(3) = "50:50"?rndxAry(4) = "54:57"?rndxAry(5) = "59:62"?'V 2 ~B@0? ??? ?? ?$?$X!Z!\ ?$?$X!Z(\?? 2 ~B@B?Z'V ?$^B@H?d'V? 4(8? 4(6?D? |??? ?&? ? 4(6? 4(8??-Error. cmd_calc1_showHideCalc_Click. at step= V F?Err no= H!J?.  H!L'( ( P?ErrorA@N?D? o??? ?x ??! ??!<(>o??? ???&? ]? ?8?P?h]??? ~.z? 'V?@format the cell with scientific notation or number with decimals?"ws.Unprotect (glob_sheet_password)?- If Range("m2_calc1_result").Value < 1# Then?= Range("m2_calc1_result").NumberFormatLocal = "0.00E-00;"?Else?5 Range("m2_calc1_result").NumberFormat = "#,##0.00"?End If? ws.Protect (glob_sheet_password)?d'V?D? |??? ?&? ? ?"Error. Worksheet_Change. in sheet: ??!? . at step= V F?Err No.= H!J?.  H!L'( ( P?ErrorA@N?D o?? ???? Macro??]??]??]?]?(]?@?X]?? ?p?? ??????]???num_selection =]?(? 'V? ~.z? 4(6? 4(8?$X!Z!\'??MsgBox Is_hidden?m2_num_selection z%^!>'??MsgBox num_selection?step = 9? rfocus = "A7"?" Application.EnableEvents = False?# Application.ScreenUpdating = False? 'V? '?? Application.EnableEvents = False?36:46?+??47:57?+??58:68?+??69:79?+??80:90?+??91:101?+??102:112?+??113:123?+??124:134? +??135:145? +??If Is_hidden = True Then?42:43?+??53:54?+??64:65?+??75:76?+??86:87?+??97:98?+??108:109?+??119:120?+??130:131? +??141:142? +??Else?End If?ARows("7:31").EntireRow.Hidden = Not Rows("7:31").EntireRow.Hidden?CRows("39:41").EntireRow.Hidden = Not Rows("39:41").EntireRow.Hidden?Application.EnableEvents = True?'V 2 ~B@0 ?? ?? ??? ??? ?$?$X!Z(\ ???? ?$?$X!Z(\d???k??x??p?? $?$X!Z(\ ????? $?$X!Z(\d??k??d??? ??? ?? ?? ?$?$X!Z(\ ???? ?$?$X!Z(\d???k???????If num_selection = 10 Then? do nothing?Else? ?? ?? ??? ?$?$X!Z(\??k???P Rows(rndxAry(rndx)).EntireRow.Hidden = Not Rows(rndxAry(rndx)).EntireRow.Hidden? Next?Z'V?m2_num_selection$^B@H?d'V 2 ~B@B? 4(8? 4(6?D0|??(?& ? 4(6? 4(8??-Error. cmd_calc1_showHideCalc_Click. at step= V F?Err no= H!J?.  H!L'( ( P?ErrorA@N?Dh?row_num = ActiveCell.Row?row_valid = row_num + 3?MsgBox row_num?MsgBox row_valid?(num_selections = Range("AL" & row_valid)?MsgBox num_selections?hcolumn_index = Array("AD", "AE", "AF", "AG", "AH", "AI", "AJ", "AK", "AL", "AM", "AN", "AO", "AP", "AQ")?c'ol_start = column_index(0)?0col_for_valid = column_index(num_selections - 1)?Range("E" & row_num).Select?Selection = "--Select Gas--"?With Selection.Validation? .Delete????? .Add Type:=xlValidateList, AlertStyle:=xlValidAlertStop, Operator:= ' xlBetween, Formula1:="=$" & col_start & row_valid & ":$" & col_for_valid & row_valid & ""? .IgnoreBlank = False? .InCellDropdown = True? .InputTitle = ""? .ErrorTitle = ""?.InputMessage = ""?.ErrorMessage = ""?.ShowInput = True?.ShowError = True?End With?Application.EnableEvents = Trueo???????x??????Attribute VB_Name = "She@et6" ?Bast0{000?20820- C$0046}|Global!?Spac?False dCreatablPre declaId?TruBExposeTemplateDeriv$?Bustom izD2Control??Comb?o_works??LinkList, 2150, MSForms?, Box???&cmd_calc1_showHideGuid, P1185?, &mandButton?(Number _Setsle?cO1017Rt?(C@,@'94, 3:clearValue?K171, ??O????=68? t_oh7? u?BF?BC48 i n D?"ppbFv$ dC49?C?50?1?2??$?D5?"?5j????666 ?8C63???M|C7: ??QC?7? 4C7? ?? ?74?D?}u8: ?r8{? ? 8? ?? 8? W+D?u9: o?r9? ? 9Ϗ ?? 96???D?u10J ?g ??10? ? 10? ?? ?107??D ??1? ??1 ??1? ? ?1? ?? ?p??nD ??2? ?1? ??2? ? 2? ???nwC12Ib?;nD ??3? ?1? ??3? ? 3? 7?:o?4?b?D1? ?'ɔl???'ߢ???٢??? Y1??Oǁ?? ??????'?O??rror GoTo e@rr_sub? B Q?stepq?Integer, @strMsg!S0?ng? rndxAry(12)?AVarianp?q???er, rndxMax As Integer  (Dim r focus?String|num_selecti,on??wzWo?rksheet? ? step = 9 ?= "A 7" Applica|.EnableEvent?sDFalse+ %ScreenU?pd4ng??B?10???= ? '?=??Set ??= A??veS? ??=?.Range("m2_ ").Valuk-?'PAry(1)?i"7:31? ?? 42:43? 2? 53:54L3B64:65L4B75:76L5B86:8?kG 6B97:98? 7B108P:109?8?1?9:120?9?P30:1?;04 1:142'RPows(?G)@?tire?.Hidden@NNot ??[?39:41?eEn C??lTr|D?2J???.@Unprot? @(glob_B?_password?)H? For?D!?1 To?Q'+? 1?b?L?)[(G\IcNex? ;??9?Cc??).?Sb???D10d??$Pr$ ?2?z???g7Kexit_Psub:?E? Sub err?? ??GrMs?"Error. cmd_calc?1?Dow `eC?_C?k. atB a(=" & _C  vbCr?Lf? no?? .Number. AaDespcrip??c?B ox? !, vbOKOnly, 3CduGo`Q% HEndC$ !P@rivateA ?Combo_@\C?LinkList_Ch¨?^On ? ?\? ?,?aԢE??,D??, lng?RCLong????a#? ?? = ??u#P??book_u?? ???????s(xMe.ob#f?fi?siuPAW,?d}5 ?y9'WName??8 ? ? Wo?|?h?vo?t?QQd??C? ?9O;)K;st?6?). in ??Z:3pA4O8??Q &p3I8No._8>"_8p?C_8_8 _83=8?DGuid??D(8 ?8P??8??t`996??e1 ~?Varian|t,Cl???? ? B??`? t???CŎo*? *???J??A? ??V?r??????!??????p50:55????54:5^??59:?6?? ???u/?@?}6?????????I֚??q_?n?SG?i ??A?AE!??cϋ?¿???#?#?M?:./????t?H(???_W???8?آt?d??ep2I???r??rr.?sg??? ?*??b??!at?eKa(OrL??sn (??Z?P?q0?By?`? Targ@?K?$o?o????M-Ro?tro??Ows@? As Worksheet Set ws = ActiveSd|step ?10'format the cell with scientific notation or? numberDdecimalsFws.Unprotect (glob_?_pa?ssword)(' If Range("m2_calc1_result").Value < 1?# ThenZ2+?2NIFbLo?'?m"0.00E -00;"! '?Else ?'?&a$#,##&?#n.d`*yPx < ???? exit_sub :E Sub rr? strMsg?IError".?_Ch?S. in ?\:" & Me.Name?@". ?w?=?!_VvbCrLfA ? No6.? ?.WA. ??Descrip???%Box (, vbOKO@nly, "? o?r?NGoTo ?: ERB9 P@rivate= Pcmd__@?sl??_ClicDk(@? '? `Macro?D?im row_??Integer ?valid?N@ _seA??ԡ?col_?_??StringBQG ,???? rndxAry(12)?Variant?, ?2A D"C Max? Is_@hidden!B?oolea?e?#?~=??????R?=< 9?8c9??App@1?.Scre?enUpd?n!SF???l?Enab?leEv?????'= Rows(?7).E??re??.H?#'DM&?? L??.G|?????F? ??"@ #!x?? rfocu!"A>7?Z????m' ???'?d崃?F?A?= 淟?|? ??R)!?36:46 D$S(V= "4X7:5?%3b5P8:68l4"6P9:79,5"8P0:90,6"9?1:101L7B?102:112l8c13:123l9c24:134l10?35:?145?c"' ?iQ?Tr`?????(? w??42:4?2D'?53:5?2(c'p64:6e ?'7H5:7L12(?'6$:8l12(?7:9?2`4?108Ӡ?2(?9?,?2(30L?u4 4egv'9^Ifs??="78:31P8>? Not@?Z@s39:?4??P= l?O??t 4?J1 S?82?{???ߏ?ۏ?DP$?&ZG??10??&0?rb?? ?s?J?(?$(q?)?S?(WQ.e??}2?3??QH??? Nex4??z ? 9_ _ _ _ ?c?r*o? ??< ? 3 ?m?ȃ+ 1???/??G?? ?1Ɓ??n??:9?1P?)?!?'do?h??? ???~? a,? l??}& kFC_'?:??vH? Qrq?????:? TC9ZC?????on@QS¨?y???4?tyG/?t_G?oNoN?? ??>+ /?t?/? ?? ????C????show?enC???? ??n?o??0??? t?????[?ρ?'??C??./?Q????=??+ 3???row_num 'MsgBox? ?valid??_selections = Range("AL?" &?)z b.column_index?Array?D", "TAE FGHUIJKLUMNOP Q"?c'ol?_starth w (0for_??!?t- 1_?xE?w?).S?????'"--? Gas--" With ?.V??a? ' ?.D&te? .Add Typ e:=xl?eList, Ale?rtStyl? op, Operator:= _?'(xlBetween, Formula1:="|=$i??DL?s?v"~:??L?@8?02.IgnoreBlank?BFals?4?.InCellDropdo?wn@Tru?)putTitle"?B.ErHror? 'CM?essag?ShowIn?=?" ??'EHnd At ?vA pplics.EnableEveLnt?ȃ6 ? S ub? ?Sheet7????????????? GSheet25+????? YSheet17"????? ?ZSheet27,????????? ?C?C97$^(>?? C100:C101$^(>??C104$^(>??C111$^(>?? C114:C115$^(>??C118$^(>??C125$^(>?? C128:C129$^(>??C132$^(>??C139$^(>?? C142:C143$^(>??C146$^(>??C153$^(>?? C156:C157$^(>??C160$^(>??C167$^(>?? C170:C171$^(>??C174$^(>?ActiveSheet.Calculate? 4(8o??8?@? 4(8?2?m3c_calc1_temp_input$^(>?C?m3c_calc1_temp_input_Units$^(>?ffffff)@?m3c_calc1_MDI_in_Feed$^(>??m3c_calc1_Valves_in_gas_Service$^(>?? ?(m3c_calc1_Valves_in_light_Liquid_Service$^(>??m3c_calc1_Pumps_Agitators$^(>???m3c_calc1_Connectors$^(>?8"?m3c_calc1_Tpr$^(> ?B@?? 4(8o??????&p]????]?? ???(?@]?X? 'V?C6'?? 4(8? 4(6? 'V?'??8:35?+??'V 2 ~B@0? ??? ?? ?$?$X!Z!\ ?$?$X!Z(\??h 2 ~B@B?Z'V ?$^B@H?d'V? 4(8? 4(6?D|???&? 4(6? 4(8??-Error. cmd_calc1_showHideCalc_Click. at step= V F?Err no= H!J?.  H!L'( ( P?ErrorA@N?DHo??@?p?&0]????]??(????0]?H]?`]?x? 'V?A7'?? 4(8? 4(6? 'V? rndxMax = 10? Application.EnableEvents = False? ~.z?m3c_num_selection z%^!>'?? step = 10?'??rndxAry(1) = "8:39"?rndxAry(1) = "8:39"?42:43?+??46:47?+??49:50?+??56:57?+??60:61?+??63:64?+??70:71?+??74:75?+??77:78? +??84:85? +??88:89? +??91:92? +??98:99?+??102:103?+??105:106?+??112:113?+??116:117?+??119:120?+??126:127?+??130:131?+??133:134?+??140:141?+??144:145?+??147:148?+??154:155?+??158:159?+??161:162?+??168:169?+??172:173?+??175:176?+??'V 2 ~B@0? ??? ????&+ 1 ?$?$X!Z!\ ?$?$X!Z(\??? 2 ~B@B?Z'V ?$^B@H?d'V? 4(8? 4(6?D0|??(?& ? 4(6? 4(8??-Error. cmd_calc1_showHideCalc_Click. at step= V F?Err no= H!J?.  H!L'( ( P?ErrorA@N?Dho??`???&P]?????? ?'V 2 .B@0? 4(6? 4(8? ??!<!>$:(@ ??!<!>$:B@H?Sheets(Me.Name).Visible = False? 4(8? 4(6 2 .B@B?d'V?D`|??X?&P? ?0Error. Combo_worksheetLinkList_Change. in sheet: ??!? . at step= V F?Err No.= H!J?.  H!L'( ( P?ErrorA@N?D?o????8]?x]??]??]??]????]?? ???` ?<????? 7??3%??c??????????????????????????x7cmd_Number_Sets_Select, 1066, 0, MSForms, CommandButton6cmd_calc1_showHideGuid, 993, 1, MSForms, CommandButton5cmd_calc1_showHideCalc, 51, 2, MSForms, CommandButton3cmd_calc1_ClearValues, 8, 3, MSForms, CommandButton3Combo_worksheetLinkList, 2449, 5, MSForms, ComboBox??ME??????????????????????????????????????????? ????????????????????????????????????????????????????????????????????????????????????????????????PSL????S????S?????, ??m3c_calc1_Connectors$^(>t??m3c_calc1_Tpr$^(>??m3c_calc1_sv_measured$^(>??C55$^(>??C58:C59$^(>??C62$^(>??C69$^(>??C72:C73$^(>??C76$^(>??C83$^(>??C86:C87$^(>??C90$^(>?2?@?x??]????num_selection =]??? 'V? ~.z? 4(6? 4(8?$X!Z!\'??MsgBox Is_hidden?m3c_num_selection z%^!>'??MsgBox num_selection?step = 9? rfocus = "A7"?" Application.EnableEvents = False?# Application.ScreenUpdating = False? 'V?'?? Application.EnableEvents = False?40:53?+??54:67?+??68:81?+??82:95?+??96:109?+??110:123?+??124:137?+??138:151?+??152:165? +??166:179? +??If Is_hidden = True Then?42:43?+??46:47?+??49:50?+??56:57?+??60:61?+??63:64?+??70:71?+??74:75?+??77:78? +??84:85? +??88:89? +??91:92? +??98:99?+??102:103?+??105:106?+??112:113?+??116:117?+??119:120?+??126:127?+??130:131?+??133:134?+??140:141?+??144:145?+??147:148?+??154:155?+??158:159?+??161:162?+??168:169?+??172:173?+??175:176?+??'V 2 ~B@0 ?? ?? ??? ??? ?$?$X!Z(\ ???? ?$?$X!Z(\d??( k?? ?? ?? $?$X!Z(\ ?????$?$X!Z(\d??? k??? d??? ? ??? ?? ?? ?$?$X!Z(\ ???? ??$?$X!Z(\d??@ k??8 ??0 ?If num_selection = 10 Then? do nothing?Else? ?? ?? ? ?? ?$?$X!Z(\???k????Z'V?m3c_num_selection$^B@H?d'V 2 ~B@B? 4(8? 4(6?D8|??0?&(? 4(6? 4(8??-Error. cmd_calc1_showHideCalc_Click. at step= V F?Err no= H!J?.  H!L'( ( P?ErrorA@N?Dpo??h?? ??! ??!<(>o??@????8?????Attribute VB_Name = "She@et7" ?Bast0{000?20820- C$0046}|Global!?Spac?False dCreatablPre declaId?TruBExposeTemplateDeriv$?Bustom izD2Control??cmd_Number_Setslect, 1066, 0, MSForms, CommandButton???(calc1_showHideGuid, 9,93+B(C/, 51, 2?ClearValueq?78, (?;?Eb?o_works??LinkLis@P02449) (boBoxOOption @{lici?t P?t?v? Sub Ae?P?(_C? k() ? App?a?.En?zEven3).Sea?y???wYL/? ?????1exitq-:??E??W?.t?!?!?g??Gstr2?)E=?5.H???qc?8. ?at?6=" &? _? ?& vbPCrLf?"? lnob?.?ȁ. ?1Descr~i?3?:`?` ,?OKOnly,? ?or?*???cIfjE Ew ѶEE? EEE? ?,q-?4oE)D,"2oE ???E??num_^s?)??WOw?IW?˂?SU/9?JA?q? #./K/K/K  ?4H'?.?dxMax = 10 'Application.Enabl?eEvents??False?? Set w8ActiveSheet8num_se$le.onzws.Range("m3c_ :").pValu [D'0stepB?rn?3?Ary(1)'"8:39"; 42:43?? 2&46:47? 3? 9:5.0? ?6?4?56:5?5? 60:61?)6? 3:6 4?)7?70:7??8? 4:75?)B9? 7:78?)1B084:8?1??R8:8?RE71F`91:92??G98:9??F102(:10\1CG10?56??I11?1??H116:1 1M^1?I119:?12?m1?K12? 2?2?J130:13?`2CK133K?o2CM14?4?CL144:14e?b2?L47r25DN5?5??L58(:15d2d&61?:16?92$'6?V6?d&72723?d&7:7 :?? ?f?d|2$z?.Unprot ? (g lob_s??_password)a?For T? To ?* 3 0'+ 1caRo8ws(???))!?tire .Hidde??Not2 _en ?Nefx???Pr~d 9d ?rfocus8).S??? ?10g?c8?Tr???ScreenUpd??ng?'?exi@t_sub:? E? Sub e?rr?? ???ʧ strMs!"Error. cm?d_calc1`>$ow?2eC?_C?@?k. at A ?=" & _C?;& vbCrL?f@? no?? ?.Number . AaDesc8rip??c?Box? !,? OKO`nly, Cd?G&o M% !End?$ Private? Com(bo_?Uk?WLinkList_C?h??XOn ?XG? ?,?DimAs Integer,D @String, lng?RCLo??)??C a#"?DHU7 +Workboo?k?7?7  ?$H?/ ?? 4A??s(M"8?C88 ?|888C9?81E#@_Ы?s@A?3E(p878rowa??447 ?uvalid?+g?:scol_fo?r_?e9Ar8?=???b????Var`iant,?op2?(5w?x ?!?@aZIs_h3o?B oolea0m'? '[=?0?pQ+?B!S?D9??SO??E??2?Ca$y_?[ɗ ?=?{7?}s '?%?c ,ο˔ͷ˿???̒"N'P?}?K"A??????R '?WI|NK?E??????%`??? ?߆q?)?? ?5??ӯ??6??????8]?s??82:9-??9p?n0??`?2M??2?P?3mD?3A??4??50?6?4?16?7??S'If cI)!b Th;?2????y2(#???34?C2(??̳ry2(5) = "60:61" rndx A?6?3:64 h ?7@70:7?v844:75?B947:78V1B0!84:8<1B18:89X1?291:92Y?3!8:9=4??102:103?-у?105?6?.?411? 1? ??11`6:117?/?1?19:120?/??T12? 2? 2??1?30:13??2??X133??2?O14@4O?N144(:14?e2DO47?@?u2?P5@5OADO58:15Ng2ADO61:16Tw2??P6@6ODO7@g?7Ng3DO7?w7?w!üstep?20?CActiveSheet.Unprotect ?(glob_sA_password)?If nu m_sel? ion?10 The?nI For ??A To?  Rows(????)).@Entire@. HiddeFa8lseC ???Is?_hETrue??!? 2 A? E? @End If?N?ext#?? (?}5? ` ??!2(:? c???1 ?+ 1?JA3_2 .?_2? C2 * 3? o_c??3'??S'd?Qothing?#'x%+ ?$AY1?h??%?W?m?L ? ??u9?uRang?e("m3c_?p").S?q)?1f0 I~Pr~"?A?pplicat`}?sableEve8nts@{g?Sc?reenUpd` ng?Kexit?_sub:?E? Sub ernr?  n BstrMs1 "Error. cmd@_calc10Oo?wPGeC?_C @k. at ?=?" &? _? qF& vbCrLfc?? nobp.@Number?. ?1Descripa3pBox ` ,?OKOn0ly, ? TtGo??S?Q"1?#? ?Privateq? Work?[?`(?[Me.Combo_?\#LinkList.Val T= Nam ?V ?? 'V? ~.z? 4(6? 4(8?$X!Z!\'??MsgBox Is_hidden?m5b_num_selection z%^!>'??MsgBox num_selection?step = 9? rfocus = "A7"?" Application.EnableEvents = False?# Application.ScreenUpdating = False? 'V?'?? Application.EnableEvents = False?35:48?+??49:66?+??63:76?+??77:90?+??91:104?+??105:118?+??119:132?+??133:146?+??147:160? +??161:174? +??If Is_hidden = True Then?40:40?+?? rndxAry2(2) = "48:51"?54:54?+?? rndxAry2(4) = "61:64"?68:68?+??rndxAry2(6) = "74:77"?82:82?+??rndxAry2(8) = "87:90"?96:96?+??rndxAry2(10) = "100:103"?110:110?+??rndxAry2(12) = "113:116"?124:124?+??rndxAry2(14) = "126:129"?138:138?+??rndxAry2(16) = "139:142"?152:152? +??rndxAry2(18) = "152:155"?166:166? +??rndxAry2(20) = "165:168"?rndxAry2(1) = "46:46"?42:45?+??rndxAry2(3) = "59:59"?56:59?+??rndxAry2(5) = "72:72"?70:73?+??rndxAry2(7) = "85:85"?84:87?+??rndxAry2(9) = "98:98"?98:101?+??rndxAry2(11) = "111:111"?112:115?+??rndxAry2(13) = "124:124"?126:129?+??rndxAry2(15) = "137:137"?140:143?+??rndxAry2(17) = "150:150"?154:157? +??rndxAry2(19) = "163:163"?168:171? +??rndxAry2(1) = "41:43"?rndxAry2(2) = "52:54"?rndxAry2(3) = "63:65"?rndxAry2(4) = "74:76"?rndxAry2(5) = "85:87"?rndxAry2(6) = "96:98"?rndxAry2(7) = "107:109"?rndxAry2(8) = "118:120"?rndxAry2(9) = "129:131"?rndxAry2(10) = "140:142"?Else?End If?ARows("7:31").EntireRow.Hidden = Not Rows("7:31").EntireRow.Hidden?CRows("39:41").EntireRow.Hidden = Not Rows("39:41").EntireRow.Hidden?Application.EnableEvents = True?'V 2 ~B@0 ?? ?? ??? ??? ?$?$X!Z(\ ???? ?$?$X!Z(\? ?$?$X!Z(\d???k???????? $?$X!Z(\ ????? $?$X!Z(\?? $?$X!Z(\d?? k??d??? ??? ?? ?? ?$?$X!Z(\ ???? ?$?$X!Z(\? ?$?$X!Z(\d???k??x??p?If num_selection = 10 Then? do nothing?Else? ?? ?? ? ?? ?$?$X!Z(\???k????P Rows(rndxAry(rndx)).EntireRow.Hidden = Not Rows(rndxAry(rndx)).EntireRow.Hidden? Next?Z'V?m5b_num_selection$^B@H?d'V 2 ~B@B? 4(8? 4(6?D|???&? 4(6? 4(8??-Error. cmd_calc1_showHideCalc_Click. at step= V F?Err no= H!J?.  H!L'( ( P?ErrorA@N?DHo??@???&0]? ?8?P?h? 'V?BstrMsg = "Selected worksheet: " & Me.Combo_worksheetLinkList.Value?3MsgBox strMsg, vbOKOnly, "Next Worksheet Selection"?'V 2 .B@0? 4(6`lD??????????-??c??????????????????????????x7cmd_calc1_showHideGuid, 4177, 1, MSForms, CommandButton3Combo_worksheetLinkList, 2724, 2, MSForms, ComboBox??ME?????????????????????????????????????????????????????????????????????????????????????????????????????????????????????????????????????????????PSL????S????S?????s????s????<??<??$:(@ ??!<!>$:B@H?Sheets(Me.Name).Visible = False? 4(8? 4(6 2 .B@B?d'V?D0|??(?& ? ?0Error. Combo_worksheetLinkList_Change. in sheet: ??!? . at step= V F?Err No.= H!J?.  H!L'( ( P?ErrorA@N?Dpo??h????`????^?Attribute VB_Name = "She?et25" ?Basx0{00?020820- C$0046}|GlobaBl?Spac?False dCre atablPr@edeclaI"d?TruBExposeTemplateDer iv$?BustomizD2Control?cmd_calc1_showHideGuid, 4177, 1, MSForms, CommandBuptton???(?b?o_works?LinkList?, 2724? )?boBox?&P?hA?l Sub ?I_Click() On Error GoTo err_sub  Dim step As In@teger,r(Msg?S?ng? rndxAry(10)?Var?ian?*??Max?foc @i?!Rapnge(??"?))@@tireCo lumn.?de?nNot ?  a?Next#?P>r??6?d?7).xSel`? ??1?0??8;Cr? ?;??exit\:? ?E??d _?? ?d??M?stf?T5?l.0rC`?#r. ?atbn=" & _C& vbPCrLf@"? no?@.Num?ber. Aa?Descrip?a_cw?? !,? O?KOnly, ? ?or?V?% !8End?$)?t?_Ch?Q?B=y?, lngRC??Lon?g?????!#?fG?^'G/?L??F?:?$M?e.?.Val?M? ''?b W? ?? ??d)?? #h??book?aZR??'w??B?s(? ).?Visi?xw-?Lj?;>'W??8 ? ??5?\Wo?\h"W?oKt=W3%?H?B?1Dtt???&?|43.? in ?~:1$:(@ ??!<!>$:B@H?Sheets(Me.Name).Visible = False? 4(8? 4(6 2 .B@B?d'V?D?|????&?? ?0Error. Combo_worksheetLinkList_Change. in sheet: ??!? . at step= V F?Err No.= H!J?.  H!L'( ( P?ErrorA@N?D?o??????&?]????? 'V? 4(8?I@?4m5b_calc1_MDI_PMDI_ratio_in_the_isocyanate_feedstock$^(>?Y@?m5b_calc1_Cblnd$^(>???@?m5b_calc1_vair_input$^(>?ft3?m5b_calc1_vair_input_units$^(>????m5b_calc1_number_of_containers$^(>?Q@?m5b_calc1_Process_Temperature$^(>?F?#m5b_calc1_Process_Temperature_units$^(>?Expected result: 2.38E-05?m5b_calc1_expectedResult$^(>? 4(8?d'V?D?|????&?? ?5Error. tc0_cmd_m5b_calc1_checkValues_Click. in sheet: ??!? . at step= V F?Err No.= H!J?.  H!L'( ( P?ErrorA@N?Do??? ???&? ]?0?H? 'V? 4(8? 4(6 2 ~B@0?8:30$X!Z!\?8:30$X!Z(\?> Rows("40").EntireRow.Hidden = Not Rows("40").EntireRow.Hidden?CRows("42:45").EntireRow.Hidden = Not Rows("42:45").EntireRow.Hidden?d'V 2 ~B@B? 4(8? 4(6?D? |??? ?&? ? ?7Error. tc0_cmd_m5b_showHideCalcDetails_Click. in sheet: ??!? . at step= V F?Err No.= H!J?.  H!L'( ( P?ErrorA@N?D? o??? ?`?&? ]????? 'V? 4(8??4m5b_calc1_MDI_PMDI_ratio_in_the_isocyanate_feedstock$^(>??m5b_calc1_Cblnd$^(>??m5b_calc1_vair_input$^(>?ft3?m5b_calc1_vair_input_units$^(>??m5b_calc1_number_of_containers$^(>??m5b_calc1_Process_Temperature$^(>?F?#m5b_calc1_Process_Temperature_units$^(>?. Range("m5b_calc1_expectedResult").Value = " "??C50$^(>??C51$^(>??c52$^(>?ft3?d52$^(>??C53$^(>??C55$^(>?F?d55$^(>??C64$^(>??C65$^(>??c66$^(>?ft3?d66$^(>??C67$^(>??C69$^(>?F?d69$^(>??C78$^(>??C79$^(>??c80$^(>?ft3?d80$^(>??C81$^(>??C83$^(>?F?d83$^(>??C92$^(>??C93$^(>??c94$^(>?ft3?d94$^(>??C95$^(>??C97$^(>?F?d97$^(>??C106$^(>??C107$^(>??c108$^(>?ft3?d108$^(>??C109$^(>??C111$^(>?F?d111$^(>??C120$^(>??C121$^(>??c122$^(>?ft3?d122$^(>??C123$^(>??C125$^(>?F?d125$^(>??C134$^(>??C135$^(>??c136$^(>?ft3?d136$^(>??C137$^(>??C139$^(>?F?d139$^(>??C148$^(>??C149$^(>??c150$^(>?ft3?d150$^(>??C151$^(>??C153$^(>?F?d153$^(>??C162$^(>??C163$^(>??c164$^(>?ft3?d164$^(>??C165$^(>??C167$^(>?F?d167$^(>? 4(8?d'V?D(|?? ?&? ?5Error. tc0_cmd_m5b_calc1_clearValues_Click. in sheet: ??!? . at step= V F?Err No.= H!J?.  H!L'( ( P?ErrorA@N?D`o??X???&H]??(? 'V?& Dim step As Integer, strMsg As String]???@?x??]??]??]??? 'V?A7'?? 4(8? 4(6? 'V? rndxMax = 10? Application.EnableEvents = False? ~.z?m5b_num_selection z%^!>'?? step = 10?'??40:40?+??42:45?+??54:54?+??56:59?+??68:68?+??70:73?+??82:82?+??84:87?+??96:96? +??98:101? +??110:110? +??112:115? +??124:124?+??126:129?+??138:138?+??140:143?+??152:152?+??154:157?+??166:166?+??168:171?+??'V 2 ~B@0? ??? ????&+ 1 ?$?$X!Z!\ ?$?$X!Z(\??? 2 ~B@B?Z'V ?$^B@H?d'V? 4(8? 4(6?D@|??8?&0? 4(6? 4(8? ?7Error. tc0_cmd_m5b_showHideCalcDetails_Click. in sheet: ??!? . at step= V F?Err No.= H!J?.  H!L'(????? strMsg = "Error. cmd_calc1_showHideCalc_Click. at step=" & step ' & vbCrLf & "Err no=" & Err.Number & ". " & Err.Description ( P?ErrorA@N?D??&?o????? ??! ??!<(>o????????????{?Attribute VB_Name = "She?et17" ?Basx0{00?020820- C$0046}|GlobaBl?Spac?False dCre atablPr@edeclaI"d?TruBExposeTemplateDer iv$?BustomizD2Control?tc0_cmd_m5b_showHideCalcDetails, 1, 0, MSFormCommandButton ???+c?'1_clearValue=#2,?*?>?L3, @????tO=O= //?=?=?!???~?~?=9o `? mandButton?1?<B?? I8shW?De ?tails_Click. in sheet:" & Me.Name$". at `step=` _ & v bCrLfREr`r No.N.?Number?v&Description?Msg?Box`r ,MOKOnly, "".or"%GoTo exit_sub End S Private tc0_cmd_m5b_calc1_clearValue?() O?n [ Urr*?hDim?u As Integer,?M Strin?gI??= 10(App??al.EnableEvents = False??Range("SMDI_Pr _in_the_isocyan?n_feedstock"<).g+<&Cblnd?vairрput #?(G @_units? "Xft3?i#n€_@of_con??ner?0?Process_Tem?pe@Eurea)?%?+F+' N+expectedRe?sul?E" 8JG?C50%C51hc52d OWC?53C55Y J"B ?64? 6q? c66X??6:7?99 ??78?? 7? c8x?Pr ivate W?ork?p"\?(?p??/Combo_@sCLinkLis?t.Value?K4 rndxAry5(12) As Variant]????]????num_selection =]??? 'V? ~.z? 4(6? 4(8?$X!Z!\'??MsgBox Is_hidden?M5a_num_selection z%^!>'??MsgBox num_selection? 'V?'?? Application.EnableEvents = False?46:67?+??68:89?+??90:111?+???112:133?+??134:155?+??156:177?+??178:199?+??200:221?+??222:243? +??244:265? +??If Is_hidden = True Then?54:64?+??76:86?+??98:108?+??120:130?+??142:152?+??164:174?+??186:196?+??208:218?+??230:240? +??252:262? +??'V 2 ~B@0 ?? ?? ??? ??? ?$?$X!Z(\ ???? ?$?$X!Z(\?,Rows(rndxAry5(rndx)).EntireRow.Hidden = Trued??pk??h??`?? $?$X!Z(\ ????? $?$X!Z(\?+R'ows(rndxAry5(10)).EntireRow.Hidden = Trued???k???d???? ??? ?? ?? ?$?$X!Z(\ ???? ?$?$X!Z(\?,Rows(rndxAry5(rndx)).EntireRow.Hidden = Trued??k?????If num_selection = 10 Then? do nothing?Else? ?? ?? ? ?? ?$?$X!Z(\???k????Z'V?M5a_num_selection$^B@H?d'V 2 ~B@B? 4(8? 4(6?D|???&? 4(6? 4(8??-Error. cmd_calc1_showHideCalc_Click. at step= V F?Err no= H!J?.  H!L'( ( P?ErrorA@N?DHo??@??&0]?X?p????? 'V?BstrMsg = "Selected worksheet: " & Me.Combo_worksheetLinkList.Value?3MsgBox strMsg, vbOKOnly, "Next Worksheet Selection"?'V 2 .B@0? 4(6? 4(8? ??!<!>$:(@ ??!<!>$:B@H?Sheets(Me.Name).Visible = False? 4(8? 4(6 2 .B@B?d'V?D?|????&?? ?0Error. Combo_worksheetLinkList_Change. in sheet: ??!? . at step= V F?Err No.= H!J?.  H!L'( ( P?ErrorA@N?D?o??????&?]???? 'V? 4(8???@?M5a_calc1_Aopen$^(>?(@?M5a_calc1_Duration_of_open$^(>?4@?M5a_calc1_Airflow_Speed$^(>?miles/hr?M5a_calc1_Airflow_Speed_units$^(>??R@?%M5a_calc1_Temperature_of_Process_Area$^(>?F?+M5a_calc1_Temperature_of_Process_Area_units$^(>?I@?M5a_calc1_Percentage_MDI$^(>?ERange("M5a_calc1_expectedResult").Value = "Expected result: 8.38E-04"? 4(8?d'V?D?|????&?? ?5Error. tc0_cmd_M5a_calc1_checkValues_Click. in sheet: ??!? . at step= V F?Err No.= H!J?.  H!L'( ( P?ErrorA@N?Do????(?&?]?h??]????????]?]?]?0? 'V?A7'?? 4(8? 4(6? 'V? rndxMax = 10? Application.EnableEvents = False? ~.z?M5a_num_selection z%^!>'?? step = 10?'??If Is_hidden = True Then?54:64?+??76:86?+?      ?        ????g       *    ! " # $ % & ' ( )  + , - . / 0 1 2 3 4 5 6 ????8 9 : ; < = O ? @ A B C D E F G H I J K L M N 7 P Q R S T U V W X Y Z [ \ ] ^ _ ` a ????c d e f ? ? j < k l m n o { q r s t u v w x y z ????? ????~  ? ? U???? ?3??!???c??????????????????????????x2Combo_worksheetLinkList, 719, 0, MSForms, ComboBoxCtc0_cmd_M5a_calc1_showHideCalcDetails, 2, 1, MSForms, CommandButton;tc0_cmd_m5a_calc1_clearValues, 3, 2, MSForms, CommandButton=tc0_cmd_M5a_calc1_showHideGuide, 4, 3, MSForms, CommandButton4cmd_Number_Sets_Select, 5, 4, MSForms, CommandButton??ME??????????????????????????????????????????? ????????????????????????????????????????????????????????????????????????????????????????????????PSL????S????S????? ?@X ?0? ? L? ? ?????  ?( ?0 ?8 ?@ ??H ?? ?? ?"??? ?????? ?????(? ?????H? ?????P?X? ????? ????? ????? ?????`? ????? h? ????? ????? x? ?? ??????? ????? ?? &?? ????? ??(?? ????? ????? ????? ?(? ????? ????? ????? 0? ????? ?????P?h??????????????(? ?????@?H?"X?2?? ????????????? ??????? ????? ?? ??? ? (? 8?tH????? ????? ????? ????? ??????? ????? (?? ????? ? ????? ( ? ????? H? ????"?X?`?h?x? ?? ???? ?????.?? D?? J(? Jx??? ?? ???? ????? ????? ???????????????? ????"???????? ? ??????8?X?x??????????8? ?????PX?J??L??JH?P??J?? ????? 8?H?P?X?`??h??? ? ????? ????"?(?0? ?????H? ????????X???x?]?@]?X]?p]??]????]?? ???? ??? ?@?? ?x?f,?98:108?+??120:130?+??142:152?+??164:174?+??186:196?+??208:218?+??230:240? +??252:262? +??'V 2 ~B@0? ??? ????&+ 1 ?$?$X!Z!\ ?$?$X!Z(\??@ 2 ~B@B?Z'V ?$^B@H?d'V? 4(8? 4(6?D?|????&?? 4(6? 4(8??-Error. cmd_calc1_showHideCalc_Click. at step= V F?Err no= H!J?.  H!L'( ( P?ErrorA@N?D o???"Private Sub CommandButton1_Click()?End Sub?"Private Sub CommandButton1_Click()?End Sub?P?&?]????? 'V? 4(8? 4(6 2 ~B@0?7:41$X!Z!\?7:41$X!Z(\?=Rows("50").EntireRow.Hidden = Not Rows("50").EntireRow.Hidden?CRows("52:53").EntireRow.Hidden = Not Rows("52:53").EntireRow.Hidden?CRows("55:57").EntireRow.Hidden = Not Rows("55:57").EntireRow.Hidden?d'V? 4(8? 4(6 2 ~B@B?D? |??? ?&? ? ?=Error. tc0_cmd_M5a_calc1_showHideCalcDetails_Click. in sheet: ??!? . at step= V F?Err No.= H!J?.  H!L'( ( P?ErrorA@N?D( o?? ???& ]??? 'V? 4(8??C47:C49$^(>??C69:C71$^(>??C91:C93$^(>?? C113:C115$^(>?? C135:C137$^(>?? C157:C159$^(>?? C179:C181$^(>?? C201:C203$^(>?? C223:C225$^(>?? C245:C247$^(>?ft/sec?7D49, D71, D93, D115, D137, D159, D181, D203, D225, D247$^(>?D?7C50, C72, C94, C116, C138, C160, C182, C204, C226, C248$^(>?F?7D50, D72, D94, D116, D138, D160, D182, D204, D226, D248$^(>?2?7C51, C73, C95, C117, C139, C161, C183, C205, C227, C249$^(>???????@?7C52, C74, C96, C118, C140, C162, C184, C206, C228, C250$^(>?c?7C53, C75, C97, C119, C141, C163, C185, C207, C229, C251$^(>? 4(8?d'V?D?|????&?? ?5Error. tc0_cmd_M5a_calc1_clearValues_Click. in sheet: ??!? . at step= V F?Err No.= H!J?.  H!L'( ( P?ErrorA@N?D?o????0 ??! ??!<(>o????????????q?Attribute VB_Name = "She?et27" ?Basx0{00?020820- C$0046}|GlobaBl?Spac?False dCre atablPr@edeclaI"d?TruBExposeTemplateDer iv$?BustomizD2Control?Combo_works?LinkList, 719, 0, MSForms, ?Box?&tc0_cmd_M5a_calc1_show HideC?Detail?$2, 1 ,mandBuPtton?.m?.clearValu?e@3, ?+j ?,Gu., 4, ???ANumb?er_Setshlec?U5B?O@ption ??licit P{} Sub S_C k() Dim row_num As ?Integer?`validN@ _se?'??col?_for_?S?݄ngstep?, strMsg?? rndxAr y(12)?Va?rian@C?2 34  ', ?? 5L? AD"?MaxhIs_@hidden!B?oo`Ln '@??$=?ws?Wh 6 ?"= 9? a? A ?= Act xb??(App`8a??.ScreenUpd??ng?t?| ?EnA|Events?c '= Rows(7).En?tire?.?r?m#'@6@{ &? L?.Range("?e?").?Bq%? ?#? A?$10?a8?2= 2??'_? ? dA(1) #"46:>6A?% Q??68X:89??)3b9?0:111L4B?112:133l5c34:155l6c56:177c78:19M8b200:2 2m9c22:24m10?44:26?##?'If??=@$?? The@]A!?D%?s? 54:$64 2(?(768:86M?(?08?m)2?,30?$)?4?,52?D)6?,?7??8p9???8:21 ?3??4 ?5?6 E=t,?*?>.Unp?rot?_ (gp??@q ?_passpw>dP[PZ3?10~y?N? To ??6??>?(q)??o??EQO!e?}2??CE?S?1'??5oo?E"??@@End If?N?ex?q?????????@SD@00??n?R'?VT?h_??e= ????ſm?{+ 1????Ic1 ?s??|??DeO???_U?C] AM?3 'd?2?othi??#'??r?5???6?j '?? ? ? ?,?q?,?D9?zq_w?DКPwS??3Yt10?)IPr?II0 ?w??,I΋g+ exit_shub:cE?!?? errx???/? 0?z?G??`Erpror.ⴏ??. atЬep="d &? _? ?&? vbCrLf?b"? nob?.3S??. ?1De?scri??3$? ,?OKOnly$, ?orDoGo?]? 1#Sub??"I???2?_Ch???fO? ?Ò"g?O?, lngRC??Long??E?11C?'?^'??*??&?:BM?e.o b U??u??յ, vbOKOnly, "Next Worksheet Selection"  step P= 204AZve?book.U nprot? ( glob_?_password)?fpplicaf.ScreenU$pdngXFalse'EnableEvents %+S?s(Me?.Combo_n?LinkList.Value)`.Visi?$?!T?ru4&??8'??Nam?,?a?A?x??d?B ???P??3?A?10??C exit_sub :E? Sub rr?strMsh"Error. ?Y_Chan?ge. in B?:" & ?eI@@". at #=[B%_??&?CrLfA  No.? ?.Number???Despcrip??)B? End?< A?Private? tc0_cmd_M5a_calc1_check?B?s_C?k(???On ? C?NC$Dim?; As Integer,?'?String? BC= 1ח???RA]("?)Aopxen"?????~0?0#??Dur?qP_of_?2?Airflow_S?peed(2? *@_units?"?miles/h?4A?Tempeu re@_cess _Area?757??FDE?Perc??age_MTDI5?'nexp??edResHulth"E$ rB: 8.38?E-04?6??g??G?G?z⻮z?]k_{?p_{rr_{_{??_{ ?zshowHideC@|Det?ail?{??3_|F|rndxAry(30)?Var?iant, ??f?Maxh?H ?focus????num_sE??? ~w?????_t&9?r= "A7ϒ+??+?| Yo??g???.?'??7Tf'?? SS?P??= ??B~?K?= ws.x>?>?_'? = 3?_3d ?'If Is_hidde?n? Then?OS?%1)?"?54:6?D?2?`76:86?F?3??98:108?4?120:13 0?5?42:152?6?64:17?7?86:19?8?208(:21?9?30h:24?1 5?(2?52:26??:3?4???o?ѥm?Flor?:?& ???!*? 1 '+ 1d??Rows(Eq)).Entire?.?GcNot? ???SQ??X+?.??t= 49T'?,??<).ٮ????>?S@c'?s50_?_vB"C?D;2:53e??eRow.Hidden = Not ?s("52:53").En?tir? ?'?5:57H ?CH?step.100Appli@cation{ableEventBs#True$ScreenUpd 3ng &ctiveSheet.Protect (@glob_s_password)?*?exit_Psub: E Sub errA? strMs;"Error. tc0_cmd_M5a_calc1I6ow??eC?Details_C?rk. in E:" & Me.Name?". hat ?= ??_?C??& vbCr?Lf??:??.???.Number?!?? Descri?p??"?XBox0?],@OKOnl(y, 1"C GoTo ?A End@ Private??;cle?arValue?9"(XOn ?"or? C?P?Dim?: As Inte0ger,?&?St0ring? BB= ?1?FalsD??Range("C?47:C49?B(????69:C7?1?91:C9A??113:C11?5W135@3?%?5)15X)17I?)18?)20*2?0X*22@*228d24 240j*D?49, D71??93???37?>5a `??25?? "ft/secOE150, C$72?94?11R6?38?6a1?8?20?22??248/68? *D D D D1? D1 D D ?D D "FM??C7?C9??>`?C13`C16a$18?20?22U?2?O5?O5!7U9?1?4?6?a18?0?2??250h7.2?TC57?9?1??4?6a18?J0?2?25 K9?9 ???`?u????b???_.???p??|rr??????)?k?W?orkC?AA?@?A?A?`?Combo_??CLinkLi?st.e??? J?Sheet11$???? ?BSheet12????-????> _USheet23?????????????? Sheet14????p y^!>'??MsgBox num_selection?step = 9? rfocus = "A7"?" Application.EnableEvents = False?# Application.ScreenUpdating = False? 'V?'?? Application.EnableEvents = False?35:46?+??47:58?+??59:70?+??71:82?+??83:94?+??95:106?+??107:118?+??119:130?+??131:142? +??143:154? +??If Is_hidden = True Then?40:43?+??52:55?+??64:67?+??76:79?+??88:91?+??100:103?+??112:115?+??124:127?+??136:139? +??150:153? +??Else?End If?ARows("7:31").EntireRow.Hidden = Not Rows("7:31").EntireRow.Hidden?CRows("39:41").EntireRow.Hidden = Not Rows("39:41").EntireRow.Hidden?Application.EnableEvents = True?'V 2 ~B@0 ?? ?? ??? ??? ?$?$X!Z(\ ???? ?$?$X!Z(\d??xk??p??h?? $?$X!Z(\ ????? $?$X!Z(\d??k??d??? ??? ?? ?? ?$?$X!Z(\ ???? ?$?$X!Z(\d???k???????If num_selection = 10 Then? do nothing?Else? ?? ?? ? ?? ?$?$X!Z(\??k????P Rows(rndxAry(rndx)).EntireRow.Hidden = Not Rows(rndxAry(rndx)).EntireRow.Hidden? Next?Z'V?m4b_num_selection$^B@H?d'V 2 ~B@B? 4(8? 4(6?D |???&? 4(6? 4(8??-Error. cmd_calc1_showHideCalc_Click. at step= V F?Err no= H!J?.  H!L'( ( P?ErrorA@N?DXo??P???&@]? ?8?P?h? 'V?BstrMsg = "Selected worksheet: " & Me.Combo_worksheetLinkList.Value?3MsgBox strMsg, vbOKOnly, "Next Worksheet Selection"?'V 2 .B@0? 4(6? 4(8? ??!<!>$:(@ ??!<!>$:B@H?Sheets(Me.Name).Visible = False? 4(8? 4(6 2 .B@B?d'V?D?|????&?? ?0Error. Combo_worksheetLinkList_Change. in sheet: ??!? . at step= V F?Err No.= H!J?.  H!L'( ( P?ErrorA@N?Do??????&?]????? 'V? 4(8?I@?4m4b_calc1_MDI_PMDI_ratio_in_the_isocyanate_feedstock$^(>?Y@?m4b_calc1_Cblnd$^(>???@?m4b_calc1_vair_input$^(>?ft3?m4b_calc1_vair_input_units$^(>????m4b_calc1_number_of_containers$^(>?Q@?m4b_calc1_Process_Temperature$^(>?F?#m4b_calc1_Process_Temperature_units$^(>?Expected result: 2.38E-05?m4b_calc1_expectedResult$^(>? 4(8?d'V?D?|????&?? ?5Error. tc0_cmd_m4b_calc1_checkValues_Click. in sheet: ??!? . at step= V F?Err No.= H!J?.  H!L'( ( P?ErrorA@N?Do?????&?]?0?H? 'V? 4(8? 4(6 2 ~B@0?8:30$X!Z!\?8:30$X!Z(\?> Rows("40").EntireRow.Hidden = Not Rows("40").EntireRow.Hidden?CRows("42:45").EntireRow.Hidden = Not Rows("42:45").EntireRow.Hidden?d'V 2 ~B? ?G????? M3?޽???c??????????????????????????x6cmd_Number_Sets_Select, 882, 0, MSForms, CommandButton.CommandButton1, 826, 1, MSForms, CommandButton=tc0_cmd_m4b_calc1_clearValues, 167, 2, MSForms, CommandButton?tc0_cmd_m4b_showHideCalcDetails, 161, 3, MSForms, CommandButton3Combo_worksheetLinkList, 1426, 5, MSForms, ComboBox??ME??????????????????????????????????????????? ????????????????????????????????????????????????????????????????????????????????????????????????PSL????S????S???????C48:C50$^(>??C60:C62$^(>??C72:C74$^(>??C84:C86$^(>??C96:C98$^(>?? C108:C110$^(>?? C120:C122$^(>?? C132:C134$^(>?? C144:C146$^(>?D?4C39, C51, C63, C75, C87, C99, C111, C123, C135, C147$^(>?gal?4D37, D49, D61, D73, D85, D97, D109, D121, D133, D145$^(>?F?4D39, D51, D63, D75, D87, D99, D111, D123, D135, D147$^(>? 4(8?d'V?D@|??8?&0? ?5Error. tc0_cmd_m4b_calc1_clearValues_Click. in sheet: ??!? . at step= V F?Err No.= H!J?.  H!L'( ( P?ErrorA@N?Dx o??p ???&` ]??(? 'V?& Dim step As Integer, strMsg As String]???@?x??]??]??]??? 'V?A7'?? 4(8? 4(6? 'V? rndxMax = 10? Application.EnableEvents = False? ~.z?m4b_num_selection z%^!>'?? step = 10?'??40:43?+??52:55?+??64:67?+??76:79?+??88:91?+??100:103?+??112:115?+??124:127?+??136:139? +??148:151? +??'V 2 ~B@0? ??? ????&+ 1 ?$?$X!Z!\ ?$?$X!Z(\??? 2 ~B@B?Z'V ?$^B@H?d'V? 4(8? 4(6?DH |??@ ?&8 ? 4(6? 4(8? ?7Error. tc0_cmd_m4b_showHideCalcDetails_Click. in sheet: ??!? . at step= V F?Err No.= H!J?.  H!L'(????? strMsg = "Error. cmd_calc1_showHideCalc_Click. at step=" & step ' & vbCrLf & "Err no=" & Err.Number & ". " & Err.Description ( P?ErrorA@N?D??&?o????? ??! ??!<(>o????????????\?Attribute VB_Name = "She?et11" ?Basx0{00?020820- C$0046}|GlobaBl?Spac?False dCre atablPr@edeclaI"d?TruBExposeTemplateDer iv$?BustomizD2Control?cmd_Number_Setslect, 882, 0, MSForms, CommandButto.n?(?1$26 , ?.$tc0_?Nm4b_calc1_clear Value?G167, ?(?sho@wHideC?D`etailB?+3?>bo_works?LinkLiRsS14A5?boBoxROption ~lic?it P?wA?y Sub h_C k() Dim row_num As In teger?validN@ _se?z??col_f(or_?S?ng!step?, ?strMsg?? rndxAry(12)?Vari?an?B?23??6, ?Max?#Is_hid?den!Boo?E?n '@?=?4ws?W?5/ ?= 9 a??c = Act`o???App`1a?8.Scre enUpd?ng??k?s ?En?s?Events?c '= Rows(7).Entir?e?. V?#'@/??H &? L?.Range("?j?").?j%? [?#')#?"'?rfocuA"A7?`Y ?&@??' ???'?d10???A= 2?'?_? ?"V)@2"?35:46D%@YA ?47:58,3Ab59:70,4A"71:82,5A"83:94,6A"95:10M7?B107:11??8c19:13?b9c31:???1?0?43:15e?c"?'IfL?#A?? The?k?(?${A? 40:43 2?((52:55M?#(64:6I D(06:79?48:9?VC100?P?d12`?t`24:12??6?@??5@5E4E?! 'End Ifs?R>"7:31?8?> Not?@??@s39:4??Q= ?O?t ??4VK??d9?7??R?.Unprot??( (g??_?q_p?ass?rdPlQc?&?G?10?&@?b`?? To K???? (q)?T?ZQ?.e?}2?3??Q?? Nex?@Qz %_ _ _ ?_ Pd? :0?n? _+= ? 3 ?m?+? 1???/?pq?/s??[/?r??:9?QP?)?'d?(?othi??!'?re+? a,?m?+_ ?? ? F??'DT ?6B?/?i?' ???A9{???A???O?SB??"Yt?\S?E?Pr?E?E`?L?L???G=? exi@t_sub:cE??ѻ?rrx ގ?  e??Errxor.?ƒ?i͓?. atep="d &? _? ?!&? vbCrLf?b"? nob?.3??. ?1De?scrib?3T???,?OKOnly$, ?orD{Go?Z? !*Subѥ????O?st_C6hҫ?bO?? ??GoTo err?_sub Dim step As Integer,@rMsgHString?, lngRC@?Lostr>???= 10'\?= "Selected worksheet: " & Me.Combo_LinkLis?t.ValueHEBox?, vbOKOnly, "Next W?T gion"9 ?2?K Active?book?.Unprot?O? (glob_?O _pass?Jd)?!Applicat?-.ScreenUpdng ?= Fals?U?EnableEv?ents??)S?s(?).Vis?i?$?!Tr?&???C'GNameI??0? X2G! ?E? K\>P?[? F??nC Pexit?:Ey? S?????E@rror. ?_Change. xin C??I??". at??ep=[B%_?A?&@?CrLfA  No.? ?.Number???Des?crip??׷? or?C?D> End?< Private? tc0_cmd_m4b_calc1_ check?is_C?Xk(`ZOn ?b ?r??3?XF%?KR!.("?MD(I_P?r?l_in_the_is ocyan?_feedstock?"?V???a50#CA? Cblnd(1B0Vvair?p?ut?9492u ?_units??"ft3?5NnbA_of_cont?ainerI1??ecess_Te?mpe?#ure(\68???F?exp`?edRes$ul)#"E$ rB: 2.38E?-05D ?A?H|?zB׎z?^k?{?{?e??{?{%עo&?{????mandButt?on1_y@???`~??*?Set |?= A?veS?| ?=?.Range("m4b_J").Valu?6?'L,?*2?@'L???1)?>"4?0:43?TE2B?52:55L3B?64:6?a? 4B?76:79? 5B?88:91L6B@100:10? 7A?12:11M!8A?24:12?!9A?36:13M"1???148:15?#OCDP?KHh.U nprot? ( glob_B?_password)1?ForCҀ? ToLt* 1 '+ 1? cRows&(EO?))??tire@.Hidd?en4Not _?en ?Nexj??L.Pr~d 9dF?#Pco).S?y? ??8?xbTr?V??q?exit_sub:? E? Su?b err?? ???̄?st"?`DError. t?c0_cmd_?pshow?2eCalcDetails_C@?k. in bB:" & ?Me.Name ?". at?=?%_?!@& vb0CrLf!? N o.?`.Num8bercaaDe`scrip!??'?%??ac?1`T?;??'A`?no??? @?BoxD,@OKOnlyH, "`orDGo@c%; O?n ? #C;aEndC>?PriPvate ??_?t?(?p?/Combo_@sC?Lin?kList??@j4 ?num_selection =]??? 'V? ~.z? 4(6? 4(8?$X!Z!\'??MsgBox Is_hidden?m8_num_selection z%^!>'??MsgBox num_selection? 'V?'?? Application.EnableEvents = False?46:65?+??66:85?+??86:105?+???106:125?+??126:145?+??146:165?+??166:185?+??186:205?+??206:225? +??226:245? +??If Is_hidden = True Then?50:50?+??70:70?+??90:90?+??110:110?+??130:130?+??150:150?+??170:170?+??190:190?+??210:210? +??230:230? +??rndxAry2(1) = "41:43"?rndxAry2(2) = "52:54"?rndxAry2(3) = "63:65"?rndxAry2(4) = "74:76"?rndxAry2(5) = "85:87"?rndxAry2(6) = "96:98"?rndxAry2(7) = "107:109"?rndxAry2(8) = "118:120"?rndxAry2(9) = "129:131"?rndxAry2(10) = "140:142"?52:53?+??72:73?+??92:93?+??112:113?+??132:133?+??152:153?+??172:173?+??192:193?+??212:213? +??232:233? +??55:62?+??75:82?+??95:102?+??115:122?+??135:142?+??155:162?+??175:182?+??195:202?+??215:222? +??235:242? +??'V 2 ~B@0 ?? ?? ??? ??? ?$?$X!Z(\ ???? ?$?$X!Z(\? ?$?$X!Z(\? ?$?$X!Z(\?,Rows(rndxAry5(rndx)).EntireRow.Hidden = Trued??k?????? $?$X!Z(\ ????? $?$X!Z(\?? $?$X!Z(\?? $?$X!Z(\?+R'ows(rndxAry5(10)).EntireRow.Hidden = Trued??0k??(d?? ? ??? ?? ?? ?$?$X!Z(\ ???? ?$?$X!Z(\? ?$?$X!Z(\? ?$?$X!Z(\?,Rows(rndxAry5(rndx)).EntireRow.Hidden = Trued??8k??0??(?If num_selection = 10 Then? do nothing?Else? ?? ?? ? ?? ?$?$X!Z(\???k????Z'V?m8_num_selection$^B@H?d'V 2 ~B@B? 4(8? 4(6?D8|??0?&(? 4(6? 4(8??-Error. cmd_calc1_showHideCalc_Click. at step= V F?Err no= H!J?.  H!L'( ( P?ErrorA@N?Dpo??h??&X]?X?p????? 'V?BstrMsg = "Selected worksheet: " & Me.Combo_worksheetLinkList.Value?3MsgBox strMsg, vbOKOnly, "Next Worksheet Selection"?'V 2 .B@0? 4(6? 4(8? ??!<!>$:(@ ??!<!>$:B@H?Sheets(Me.Name).Visible = False? 4(8? 4(6 2 .B@B?d'V?D?|????&?? ?0Error. Combo_worksheetLinkList_Change. in sheet: ??!? . at step= V F?Err No.= H!J?.  H!L'( ( P?ErrorA@N?Do?????&]???? 'V? 4(8???@?m8_calc1_Aspill$^(>?(@?m8_calc1_Duration_of_spill$^(>?4@?m8_calc1_Airflow_Speed$^? ?M????? ?B?? ???c??????????????????????????x7cmd_Number_Sets_Select, 1544, 0, MSForms, CommandButton/CommandButton2, 1433, 1, MSForms, CommandButton<tc0_cmd_m8_calc1_clearValues, 235, 2, MSForms, CommandButtonDtc0_cmd_m8_calc1_showHideCalcDetails, 232, 3, MSForms, CommandButton3Combo_worksheetLinkList, 2249, 5, MSForms, ComboBox??ME??????????????????????????????????????????? ????????????????????????????????????????????????????????????????????????????????????????????????PSL????S????S?????0?0p? J?? ????? ??????? ??????? ????? (?? ????? ? ????? (? ????? @? ????"?P?X?`?p? x? ???? ?????.?? D?? J ? Jp??? ?? ???? ????? ????? ????????????????? ????"????????? ? ??????0?P?h??? ???????????????0? ?????H?`?x????????? ????????(?@?`?x??? ??????????????(?@? ?????X?p??????????? ?????? ?8?P?p????? ???????????? ?8?P? ?????h???????????? ??????0?H?`??????? ????? ??????????????????? ????"????? ??????? ??????? ??????? ??????? ????? ????? ????? ?????? ????? ? ????? ????? (? 8? ?????H? ????? P? &h? ????? ??&?? ????? ????? ????? ???? ????? ????? ????? ?? ????? ???????0?H?`?x???????????? ?8?P?h??????????????(?@?X?p??????? ????? ????? ????? ????? ?????????"??2 ? ?????H ?P ?` ?h ? ?????x ? ????? ? ? ? ?? ?? ?? ? ? ? ? ?t? ?P!?h!? ????? ????? ????? ?????p!? ????"?x!??!? ??????!? ?????????!???x?]?@]?X]?p]??]????,]?? ???? ??? ?@?? ?x?f, rndxAry5(12) As Variant]????]???(>?miles/hr?m8_calc1_Airflow_Speed_units$^(>??R@?$m8_calc1_Temperature_of_Process_Area$^(>?F?*m8_calc1_Temperature_of_Process_Area_units$^(>?I@?m8_calc1_Percentage_MDI$^(>?DRange("m8_calc1_expectedResult").Value = "Expected result: 8.38E-04"? 4(8?d'V?D?|????&?? ?4Error. tc0_cmd_m8_calc1_checkValues_Click. in sheet: ??!? . at step= V F?Err No.= H!J?.  H!L'( ( P?ErrorA@N?D(o?? ?"Private Sub CommandButton1_Click()?End Sub?"Private Sub CommandButton1_Click()?End Sub?(?&?]?h??? 'V? 4(8? 4(6 2 ~B@0?7:42$X!Z!\?7:42$X!Z(\?=Rows("50").EntireRow.Hidden = Not Rows("50").EntireRow.Hidden?CRows("52:53").EntireRow.Hidden = Not Rows("52:53").EntireRow.Hidden?CRows("55:57").EntireRow.Hidden = Not Rows("55:57").EntireRow.Hidden?d'V? 4(8? 4(6 2 ~B@B?D|??? ?&? ? ?<Error. tc0_cmd_m8_calc1_showHideCalcDetails_Click. in sheet: ??!? . at step= V F?Err No.= H!J?.  H!L'( ( P?ErrorA@N?D0 o??( ???& ]????? 'V? 4(8??c47:C49$^(>?ft/sec?d49$^(>?D?c51$^(>?F?d51$^(>??c54$^(>??c67$^(>??c68$^(>??c69$^(>?ft/sec?d69$^(>?D?c71$^(>?F?d71$^(>??c74$^(>??c87$^(>??c88$^(>??c89$^(>?ft/sec?d89$^(>?D?c91$^(>?F?d91$^(>??c94$^(>??c107$^(>??c108$^(>??c109$^(>?ft/sec?d109$^(>?D?c111$^(>?F?d111$^(>??c114$^(>??c127$^(>??c128$^(>??c129$^(>?ft/sec?d129$^(>?D?c131$^(>?F?d131$^(>??c134$^(>??c147$^(>??c148$^(>??c149$^(>?ft/sec?d149$^(>?D?c151$^(>?F?d151$^(>??c154$^(>??c167$^(>??c168$^(>??c169$^(>?ft/sec?d169$^(>?D?c171$^(>?F?d171$^(>??c174$^(>??c187$^(>??c188$^(>??c189$^(>?ft/sec?d189$^(>?D?c191$^(>?F?d191$^(>??c194$^(>??c207$^(>??c208$^(>??c209$^(>?ft/sec?d209$^(>?D?c211$^(>?F?d211$^(>??c214$^(>??c227$^(>??c228$^(>??c229$^(>?ft/sec?d229$^(>?D?c231$^(>?F?d231$^(>??c234$^(>? 4(8?d'V?D|???&? ?4Error. tc0_cmd_m8_calc1_clearValues_Click. in sheet: ??!? . at step= V F?Err No.= H!J?.  H!L'( ( P?ErrorA@N?DPo??H??&8]?H?`]???x????]??]??]?? 'V?A7'?? 4(8? 4(6? 'V? rndxMax = 10? Application.EnableEvents = False? ~.z?m8_num_selection z%^!>'?? step = 10?'??If Is_hidden = True Then?50:50?+??52:53?+??55:62?+??70:70?+??72:73?+??75:82?+??90:90?+??92:93?+??95:102? +??110:110? +??112:113? +??115:122? +??130:130?+??132:133?+??135:142?+??150:150?+??152:153?+??155:162?+??170:170?+??172:173?+??175:182?+??190:190?+??192:193?+??195:202?+??210:210?+??212:213?+??215:222?+??230:230?+??232:233?+??235:242?+??'V 2 ~B@0? ??? ????&+ 1 ?$?$X!Z!\ ?$?$X!Z(\??? 2 ~B@B?Z'V ?$^B@H?d'V? 4(8? 4(6?DX|??P?&H? 4(6? 4(8??-Error. cmd_calc1_showHideCalc_Click. at step= V F?Err no= H!J?.  H!L'( ( P?ErrorA@N?D?o????0 ??! ??!<(>o??`????X?????Attribute VB_Name = "She?et12" ?Basx0{00?020820- C$0046}|GlobaBl?Spac?False dCre atablPr@edeclaI"d?TruBExposeTemplateDer iv$?BustomizD2Control?cmd_Number_Setslect, 1544, 0, MSForms, CommandButt\on???(?2?$4 33??$tc0_?Om8_calc1_clearValue?G235, ?.(?sho@wHideCD?etail??.??bo_works??LinkLis?T2249, ?-?boBox@S?Option ?licit Py{ Sub ?i_C k() Dim row_num As Integer??validN@ 8_se|??co@l_for_?S ??ngstep?, strMsg?? rndxA@ry(12)?V`arian?B?234  ',? ? 5L? AD"1?MaxhIs?_hidden!Boo`Mn 'K@?$=?ws?W?<6 ?"= 9p a?@k ?= Act wb?Q?App`8a??.ScreenUp?d?ng?s?{ ?EnA{Events?c '= Rows(7).E?ntire?. ]ۀ#'@6?O &? L?.Ran0ge("?q?")?."r?$? ??"? !9d$10?A8?2= ?2?'?? ? DA(1)#"46?:65?k%Q??P66:8-3b8P6:10M4B1?0`2m5c2`Z4m6c?17kc 1N8c`2Un9b2`2n1v0??2?##?'If?=@$?? Th~e ]?$?D%?s? 5?0:50?(2(?(070:7N?(90 :9N?(10:1?1?)3?3?$)?`1???1????1 ? 2 ?- 2 %='\418:43T?c52?:54?s637*?w?74:76~?s85:87?c`96:98?T07.9?d18:12??s1290:131??14??4???$?$?\?$??E?3?$2:7???$2:9??$2?$w??$?3??$?5???$???$? ?$?2:21n?$? ?*?m#5:6$?m?4% ?$5@??5?2?5?5?5??5?8n5?5:20?5? ?6?X$STc?aC?t?.Unprot??( (g??_—_p?ass??d ??M0P?:jpP10^P`???? To lm??ut,?(q)?v?h|Q/X?e?}2?|???{]3__?9 4?__R'i5oobE2Ӣ@End? If?Nex@?????(?!?????А?m0?no??4pL??= ?B???=?? 'R?'???__ ??,mȿ+ 1?v?-Y???-s%?-T???Q(5?w.Hidden = True Rows(rndxAry4 )).Enti?reh?' l5&lElszEnd If?Next 'If num_selectio?10 Then&'do no?thingbpFor ?|?$+ 1 To 10? h?g?U?f*?shtep?9?4 Range("m8?_ K").Sv?S?#10?#A??veSheet.Prot?? (glob_s? _pa?ssword) "?Applica?R@yableEve8nts?'Dž Sc?reenUpd? ng? ? ex?it_sub:?BE? SubrNr??? En?)strMs?$"Error. cmd@_calc1?@o?w@?eC@_C?<@k. at ?P=?" & _?*A?& vbCrLf??? ?.Nu?mber. ??DescripǁQ??!Box?A$,OKOnly?, ?&"C Go@?J ???H P@rivateAL @Combo_?nkrLinkLis0t_ChŒ?sOn> @!@?X?Dim7As Int?eger,?% @Str`e, lngRCLong???C ?"#FO?F'/?Ued ?:?$Me.?.Val?'?&?k Wo?rc ? ?$)?d2?cbook0.Unp_dzSFa????S???ss(?!?).Visi?q*l??)k?'?Nam?e) ?8߁́?&.?_? #$?K$7???????g. in ?j~:?y?2?$?{??N??6/=OgOOOo O='\mandButton1< '?x?//??????G?2oB ???ķ??/","hB?DΦy??|@???r?"7:420.? Not ???ϳ ?"50_A?WP?;2:5>3olO?ۛ5:?57??O?&e??????/????t?????"??Bmqsh??Detail??qoCoCoC 0A??oC?oCoCoCoCoC?Ի??QM8??clear_?д Error GoTo err_@sub Dim step As Integer,@rMsg?HString?!L= 10Application.EnableEvents =? FalseJ Range("c47:C49")?.Value)Kd "ft/sHec" B51>6J8 d "F:43?< .67??]68ۘ?i6??i7?i U?i7?i8?i8?48w?4??49?4 ?49I?410510X51?0?5 ?5116K?N611?62?62?6?2?6?T3Z?Oj3_4Y4Y??1???c1چ?O5_?9?1Y?1?졋?6U??1ۇ1??1?1?9?1Y??T??1???1߈2و2و2و??S2ڈ?R2߈J2و2oD un2?oD?d??A~2oD{???d??oD? ?cz/?&?Tru?f???4exit??:?rE? S??4?ts"t?= "b?. tc0_cmd_m8_calc1@_clearB?s_C`?k. in sheet:" & Me.Name?". atm"?=??_?? &? vbCrLf?a? No.r?.?Number3?1DescripGQ?C??Box$?,?OKOnly,? $???? Ends PrivXate?fMeshowHideC?@Detail??() On_?T?? ??????rndxAry(30)?Variant<, qF?Max8C?focusi??num_?selec?~? ?w?Work????_t&9?r?$$:(@ ??!<!>$:B@H?Sheets(Me.Name).Visible = False? 4(8? 4(6 2 .B@B?d'V?D|????&?? ?0Error. Combo_worksheetLinkList_Change. in sheet: ??!? . at step= V F?Err No.= H!J?.  H!L'( ( P?ErrorA@N?D@o??8????0????²Attribute VB_Name = "She?et23" ?Basx0{00?020820- C$0046}|GlobaBl?Spac?False dCre atablPr@edeclaI"d?TruBExposeTemplateDer iv$?BustomizD2Control?Combo_works?LinkList, 3524, 1, MSFo rms, Box??P???C Sub ? _Change() On Error GoTo err_@sub Dim step As Integer,rMsg S?ng, l?ngRCLo?str???CCC?= 20?Act@LW?9book.Unprot@ect (g@v_A?>_pass@Bd?,Application.Sc?reenUpd??ngN^? EnA]?EventsK %AB?s(Me.^.Value).Vxisi??o&S?el?6C'G??I??0? I?@ABCDEFGHIJKLMNOPQRSTUVWXYZ[\]^_????abcdefghijklmnopqrstuv????xyz{|}~????????? ????? ????? x? ?? ?? ?? ?? ? 8? X? x? ?? ????? ?? ?? ????? H?? J ? ????? &p ?? ? ?????"? ? ????? ? ? ?????? ?=? ? ? ?< ?<( ?H ?P ? X ? ?????>` ? ? ?=? ?=? ?? ?? ?? ? ?????? ?= ? ?<0 ?<P ?p ?x ? ????? ? ? ????? ? ? ? ? ? ? ?????? ?<? ? ? ????? ? ????? ????? ????? ????? ????? ????? ????? V ? ????? ????? h ? ?????x ? ?????"#? ? ????? ?????? ?"? ? ????? ? ? ? ? ????? ????? ?????? ?? ?? ? ? ? ?ty?.?????? ????"? ?????? ??????? H?? :8? ?????x??? ?? ?? ????????? &?? ????? ? ?(? ?????8? ????? ?????@?H?P??X????"? ?? ?0? 8? ?????LH?(??,??0??6 ?6X?8??D?? ????? ? ?(?0?8??@??????? ????"? ??? ? (? 8?H?.X? D?? J?? ????? ????? ????? ? ????? ?????(? 8? H?X?`?h??p?? ?(? ????"? 0?8?@?P? X? ????? h????? ?????????? ?@?`? ?????x?????????? ?????0?P?p??????? ????????(?H?h??? ???????????? ?@? ?????X?x????????? ??????0?P?p????? ??????????(?H?h? ?????????????? ? ????? 8?H?`?D?????????2m??c??????????????????????????x3Combo_worksheetLinkList, 1033, 1, MSForms, ComboBox7cmd_calc1_showHideGuid, 1165, 2, MSForms, CommandButton??ME?????????????????????????????????????????????????????????????????????????????????????????????????????????????????????????????????????????????PSL????S????S?????s????s????<??<??$:(@ ??!<!>$:B@H?Sheets(Me.Name).Visible = False? 4(8? 4(6 2 .B@B?d'V?D0|??(?& ? ?9Error. sheet14. Combo_worksheetLinkList_Change. in sheet: ??!? . at step= V F?Err No.= H!J?.  H!L'( ( P?ErrorA@N?D`o??X?? ??! ??!<(>o??0???& ]? ?8]?? ?P????]??? 'V?C6'?? 4(8? 4(6? 'V?'??6:43?+??rndxAry(2) = "42:47"?rndxAry(3) = "50:50"?rndxAry(4) = "54:57"?rndxAry(5) = "59:62"?'V 2 ~B@0? ??? ?? ?$?$X!Z!\ ?$?$X!Z(\??? 2 ~B@B?Z'V ?$^B@H?d'V? 4(8? 4(6?D@|??8?&0? 4(6? 4(8??-Error. cmd_calc1_showHideCalc_Click. at step= V F?Err no= H!J?.  H!L'( ( P?ErrorA@N?Dxo??p????h??????Attribute VB_Name = "She?et14" ?Basx0{00?020820- C$0046}|GlobaBl?Spac?False dCre atablPr@edeclaI"d?TruBExposeTemplateDer iv$?BustomizD2Control?Combo_works?LinkLis?t, 1033?, MSForm?s, Box???&cmd_calc1_showH?ideGuid#@165, 2 &mandButton?(Option licit0 Prv S ub?=S_Change() Orror GoTo err_s ub Dim step As Intege?r,rMsg?S@?ng, lnHgRCLo?s?tr????Cv=?I?'? ?G?. " & Now$()?".?0. ?Select?uFc":?Me.Ti.V?alA?A%'@g?5, vbOKOnly, "Nex?t W?x?@[?]?3?20?3Act??book.Unp?rot?' (g?ƒ?w@?_pass+Fd?_Appoar.Screen?Upd?ng@?D? ? En??Even?tsK ?!??s(?@?).Visi#o^g?().C/#'???}) hc),???"?+.P?-A??Q?7? exit??`:E??i?cK?gWEAh. b?1?4Vinc:a]?4!&?]at@Qep=[?_c?&?SC?rLf! ?d.?`.NumbercaaDescr?i"??w]?or[?#?D End????Fc_?^`???N? V?a  i???_C}`ek?}??"??rndxAry(10)!?Varia>n???ƟMaxh?focus?AI??$M9?r#???C6?.XbT?Y???1?[e??dU)?"6:43?'??2?42:47?3?50:50E?4?4:5^5?9:62T? kT?E?Tw=T?v A ? |1 ?l?p?!)Rpows(Qaq)).EntireE?. wden?N?ot ???Sqb??_c ?HtM E!?>R2y?!?U??10??4?c?Tp???T(f˳T?Ot?O ???_ T ?S/?CP?#?<. ?Q??Qno??Q???Qn3?QU??Q?Q?QP?X?`??h??? ? ????"? (?0?8?H? ????? ,P? ??????? ??????? ????????? ??????? ????? ?? ????? ?? ?? ??????? ????? ?? &? ????? 8?(H? ????? p??? ???????????? ? ? ? ? ? h ? ? ? ? ? ? ? ? ? ? ? ? ? ? ? ? ? ? ? ? ? ? ? ? ? ? ? ????? ? ? ? ? ? ? ? 3 9 ? ? ? ? ? ? ? ? ? ? ? ? ? ? ? ? ????? ? ? ? ? ? ? ? ? ? ? ? ? ? ? ? ? ? ? ? ? ? ? ? ? ? ? ? ? ? ? ? ? ? ? ? ????? ? ? ? ? ? ? ? ? ? ? ? ? ? ? ? ? ? ? ? ? ? ? ? ? ? ? ?  9E??[I??|Y??c??????????d??????h`R@?RaR??D? ?FY鯜??G??,O,??????????????x=tc0_cmd_m6S_showHideCalcDetails, 2, 1, MSForms, CommandButton;tc0_cmd_m6S_calc1_clearValues, 3, 2, MSForms, CommandButton3tc0_cmd_M6S_ShowGuide, 4, 3, MSForms, CommandButton4cmd_Number_Sets_Select, 5, 4, MSForms, CommandButton2Combo_worksheetLinkList, 448, 6, MSForms, ComboBoxY鯜??G??,O,?Μ???h`R@?RaR??D???ME?????????????H?????????????????????????????? ????????????????????????????????????????????????????????????????????????????????????????????????@[L????S????S????? ???|s????s????6"?????????L????P????L????????? ????????????L????????????'??MsgBox num_selection?step = 9? rfocus = "A7"?" Application.EnableEvents = False?# Application.ScreenUpdating = False? 'V?'?? Application.EnableEvents = False?35:48?+??49:66?+??63:76?+??77:90?+??91:104?+??105:118?+??119:132?+??133:146?+??147:160? +??161:174? +??If Is_hidden = True Then?40:40?+?? rndxAry2(2) = "48:51"?54:54?+?? rndxAry2(4) = "61:64"?68:68?+??rndxAry2(6) = "74:77"?82:82?+??rndxAry2(8) = "87:90"?96:96?+??rndxAry2(10) = "100:103"?110:110?+??rndxAry2(12) = "113:116"?124:124?+??rndxAry2(14) = "126:129"?138:138?+??rndxAry2(16) = "139:142"?152:152? +??rndxAry2(18) = "152:155"?166:166? +??rndxAry2(20) = "165:168"?rndxAry2(1) = "46:46"?42:45?+??rndxAry2(3) = "59:59"?56:59?+??rndxAry2(5) = "72:72"?70:73?+??rndxAry2(7) = "85:85"?84:87?+??rndxAry2(9) = "98:98"?98:101?+??rndxAry2(11) = "111:111"?112:115?+??rndxAry2(13) = "124:124"?126:129?+??rndxAry2(15) = "137:137"?140:143?+??rndxAry2(17) = "150:150"?154:157? +??rndxAry2(19) = "163:163"?168:171? +??rndxAry2(1) = "41:43"?rndxAry2(2) = "52:54"?rndxAry2(3) = "63:65"?rndxAry2(4) = "74:76"?rndxAry2(5) = "85:87"?rndxAry2(6) = "96:98"?rndxAry2(7) = "107:109"?rndxAry2(8) = "118:120"?rndxAry2(9) = "129:131"?rndxAry2(10) = "140:142"?Else?End If?ARows("7:31").EntireRow.Hidden = Not Rows("7:31").EntireRow.Hidden?CRows("39:41").EntireRow.Hidden = Not Rows("39:41").EntireRow.Hidden?Application.EnableEvents = True?'V 2 ~B@0 ?? ?? ??? ??? ?$?$X!Z(\ ???? ?$?$X!Z(\? ?$?$X!Z(\d???k???????? $?$X!Z(\ ????? $?$X!Z(\?? $?$X!Z(\d??(k?? d??? ??? ?? ?? ?$?$X!Z(\ ???? ?$?$X!Z(\? ?$?$X!Z(\d???k?????x?If num_selection = 10 Then? do nothing?Else? ?? ?? ? ?? ?$?$X!Z(\???k????P Rows(rndxAry(rndx)).EntireRow.Hidden = Not Rows(rndxAry(rndx)).EntireRow.Hidden? Next?Z'V?M6S_num_selection$^B@H?d'V 2 ~B@B? 4(8? 4(6?D|???&? 4(6? 4(8??-Error. cmd_calc1_showHideCalc_Click. at step= V F?Err no= H!J?.  H!L'( ( P?ErrorA@N?DPo??H???&8]? ?8?P?h? 'V?BstrMsg = "Selected worksheet: " & Me.Combo_worksheetLinkList.Value?3MsgBox strMsg, vbOKOnly, "Next Worksheet Selection"?'V 2 .B@0? 4(6? 4(8? ??!<!>$:(@ ??!<!>$:B@H?Sheets(Me.Name).Visible = False? 4(8? 4(6 2 .B@B?d'V?D?|????&?? ?0Error. Combo_worksheetLinkList_Change. in sheet: ??!? . at step= V F?Err No.= H!J?.  H!L'( ( P?ErrorA@N?D?o??????&?]????? 'V? 4(8?I@?4M6S_calc1_MDI_PMDI_ratio_in_the_isocyanate_feedstock$^(>?Y@?M6S_calc1_Cform$^(>???@?M6S_calc1_vair_input$^(>?ft3?M6S_calc1_vair_input_units$^(>????M6S_calc1_number_of_containers$^(>?Q@?M6S_calc1_Process_Temperature$^(>?F?#M6S_calc1_Process_Temperature_units$^(>?Expected result: 2.38E-05?M6S_calc1_expectedResult$^(>? 4(8?d'V?D?|????&?? ?5Error. tc0_cmd_M6S_calc1_checkValues_Click. in sheet: ??!? . at step= V F?Err No.= H!J?.  H!L'( ( P?ErrorA@N?Do?????&? ]?0?H? 'V? 4(8? 4(6 2 ~B@0?8:30$X!Z!\?8:30$X!Z(\?> Rows("40").EntireRow.Hidden = Not Rows("40").EntireRow.Hidden?CRows("42:45").EntireRow.Hidden = Not Rows("42:45").EntireRow.Hidden?d'V 2 ~B@B? 4(8? 4(6?D? |??? ?&? ? ?7Error. tc0_cmd_M6S_showHideCalcDetails_Click. in sheet: ??!? . at step= V F?Err No.= H!J?.  H!L'( ( P?ErrorA@N?D? o??? ?`?&? ]????? 'V? 4(8??C36:C39$^(>?Q@?C41$^(>?F?D41$^(>??C50$^(>??C51$^(>??c52$^(>??C53$^(>?Q@?C55$^(>?F?d55$^(>??C64$^(>??C65$^(>??c66$^(>??C67$^(>?Q@?C69$^(>?F?d69$^(>??C78$^(>??C79$^(>??c80$^(>??C81$^(>?Q@?C83$^(>?F?d83$^(>??C92$^(>??C93$^(>??c94$^(>??C95$^(>?Q@?C97$^(>?F?d97$^(>??C106$^(>??C107$^(>??c108$^(>??C109$^(>?Q@?C111$^(>?F?d111$^(>??C120$^(>??C121$^(>??c122$^(>??C123$^(>?Q@?C125$^(>?F?d125$^(>??C134$^(>??C135$^(>??c136$^(>??C137$^(>?Q@?C139$^(>?F?d139$^(>??C148$^(>??C149$^(>??c150$^(>??C151$^(>?Q@?C153$^(>?F?d153$^(>??C162$^(>??C163$^(>??c164$^(>??C165$^(>?Q@?C167$^(>?F?d167$^(>? 4(8?d'V?D?|????&?? ?5Error. tc0_cmd_M6S_calc1_clearValues_Click. in sheet: ??!? . at step= V F?Err No.= H!J?.  H!L'( ( P?ErrorA@N?D?o??????&?]??(? 'V?& Dim step As Integer, strMsg As String]???@?x??]??]??]??? 'V?A7'?? 4(8? 4(6? 'V? rndxMax = 10? Application.EnableEvents = False? ~.z?M6S_num_selection z%^!>'?? step = 10?'??40:40?+??42:45?+??54:54?+??56:59?+??68:68?+??70:73?+??82:82?+??84:87?+??96:96? +??98:101? +??110:110? +??112:115? +??124:124?+??126:129?+??138:138?+??140:143?+??152:152?+??154:157?+??166:166?+??168:171?+??'V 2 ~B@0? ??? ????&+ 1 ?$?$X!Z!\ ?$?$X!Z(\?? 2 ~B@B?Z'V ?$^B@H?d'V? 4(8? 4(6?D?|????&?? 4(6? 4(8? ?7Error. tc0_cmd_M6S_showHideCalcDetails_Click. in sheet: ??!? . at step= V F?Err No.= H!J?.  H!L'(????? strMsg = "Error. cmd_calc1_showHideCalc_Click. at step=" & step ' & vbCrLf & "Err no=" & Err.Number & ". " & Err.Description ( P?ErrorA@N?D@?&8o??0????(????w?Attribute VB_Name = "She?et16" ?Basx0{00?020820- C$0046}|GlobaBl?Spac?False dCre atablPr@edeclaI"d?TruBExposeTemplateDer iv$?BustomizD2Control?tc0_cmd_m6S_showHideCalcDetails, 2, 1, MSFormCommandButton ???+c?'1_clearValue?#3,?*M?VS?VGu?+, 4, n?=Numbe@r_Setsl?ect, 5B??Fbo_works??LinkLis?448, 6A QboBox?OP?@r@t Sub ?#_Click() Dim row_num As Integer??validN@ ?_seA6ionNcol_for_%?S??ngstepH , strMsg?? rndxAry(12)??Varian?=u?23??6,b ?Max?C&I?s_hiddeBoo`Kn 'K@?=?ws!WE3 !?= 9p a?`A ?= Act?l???App`1at).ScreenUdpd?ng@iDq ?En?pEve8nts?c '= Rows(7).@Entire?.??q?#'@/?F &? L?.Ra`nge("?d?"|).Bp%? ?#' )#?"'?rfoc?uA"A7W ?&?@??' ??'?9d10??A= ?2?'??  ?"V)@2"35:<48D%@Y??49\:6A?A%3b6(3:7-4"77(:90? 5"91P:104L6B1?05:11?7c@19:132?8Ac33:149Ac47:16M1?0?6?7??"?8'IfGL?#?? T?he?k? ??!@{? ?40:4'bv?+?2(d(8:51??E54:5D??(?6?f$08:6'??74:7?E*?s82:8?;g?8?|6:N9??%00?3?1?1??C|11pR??AQ*1x24:0?s1?26?9?e"8 $??1? 3&4U?A?$52:15?1??5??&? ?4? ~2?(?/???&6?:m.?c?2:4?CgC"59:5<39t)56?=?72L:7T$3(s780:7?7?:85$:8?3(?'4:28?S ?s98?:9u6?'00?4Iw11R11=1ٌ63(?'?1E 3 &?DH?%?? 1?3?F3,73(?!?A\14??525?2??'?/5???y?X16??'?7???Y??$1:? ?s:`.K??@6?%w?I?C??"?]?9Go;000??-D1P2G?21e5?%?/?'El??I'En0d IfJ??"78:310???KNo?t??J?sI4????= ?O?T ??????ĆE???.@Unprot?? (g???P?_pa?ss?d??Qc?s?:??10t?Ԃr?? To l????,?(q)???x?Q?{?e?}2?3???]3__A 7#??i#NextS?`(??M? If Is_hidden = True Then Rows(rndxAry2(10)).@Entire`.H pf3$fEls?eAEnd?aFor ??1 To num_selectio?n + 1& ????Fa <-?D/?????qNext???'_ ?= 10??'d??othin?g?XWVA[10??WA? ?*?x A'A?? N' ?Not? P(step??913Q?>c13z63x6C^1?o?u4?>49t1?19?C15??2o?u6?>6?>tc1ک1?T?p%j1~6Y? ?? /q&qT?ruqftpt~:3l6E?~c~e3ztst????r#?.????=?? ????????r.??????????????showHideC?p?Detail??r? ?????B>'/?%?crndxAry(20)q?Varianxt, q??Max8C?focus٘?num?_selec??~??w?Work?????(9?Sr? = "A7$? '?.?? YSc?reenUpd??|ng ,???0#R'?ra??'??? ?Set ?= Aq?veS??# =?P.??q?????S?' = 2???#b a 1)?;40:<40$Q"?2:45?3?54:54?4?6:5.9?? 55?68(:68?6?70(:73?7?82(:82?8?4:8? ?9?96:496?1?/`$980:101?#11,0:0?2211.2?u[1?124:0?126??5?1?13` *311?14?5??15? 0????1`15???|16` p???B?1?`17?#'?%-?.Unprot??? (glob_>_passwor?d?߱(For?(0( 1 p? 0* 2 0'+ 1??Ro?ws(E q)) ?Ptire?.@Xd?en?Not ????SNext??Y Pr? < 49$6?;?J).S?OsS9?10?S"DV?cation.EnableEvents = Tr ue Appli?Scre enUpd?ng?exit_sub:bE Su?b err. ??p?strMs?"Error. tc0_cmd_M6S_showHideCalcDetails_C?k. in sheet:" & Me.Name?". at `step=  _?fI& vbCrLf??7 No.??.Number?!?? Des?crip?"'-?W?Uc?O1?VSFN'E??Fno*F Q?BoxI,mO?KOnly, ?R?"?=GoTo Ev? On ?6xor C?v?E nd?|??)Q??)Qy??? 9i???9a???!Qy???!Q?? A 9 i ? )?Y??Qi?????? 8?Q?????` ???????????????????????????????????????????????????????????????????????????? @?Q????`????????????????????????????????????????????????????????????????????????????? H?QI????`????????????????????????????????????????????????????????????????????????????? P?Q?????`?????????????????????????????????????????????????????????????????????????????Ta1????????????????????????????????????????????????????????????????????????????????????????????????????????????????????????????? \????` ?????????????????????????????????????????????????????????????????????????????????????????Ey??1???9m?M??W??T`? pn??$@l?=???? ?!?????!???;(??%?!???????=???A???Vp??6??????+?'??%:??%???a??Upv??5??? pn??p?:???P???:?? ?P???:?? ?P???:?? ?P???:?? ?P???:???P???:???P???:???P???:??? P???:??? P???:???4???:???4???:???4???:???4???:???4???:???4???:???4???:???4???:??? 4???:??? 4???:??????:??????:??????:??????:?? ????:??!????:??"????:??#????:??$? ???:??%? ????pn?":??&%?$@???'? kv?? ????kv??c???=?f??%k??P?@?? @?!???????=???C?6???? k??????f??%? P?@?? @?!???????=???C?6???? k?????=c??%? 4?@?? @?!???????=???C?6????=c??%? ?@?? @?!???????=???C?6????????kv????c???=?f??%k??P?@?? @?!???????=???C?6???? k?????$:(@ ??!<!>$:B@H?Sheets(Me.Name).Visible = False? 4(8? 4(6 2 .B@B?d'V?D?|??????????????޲-??c??????????????????????????x2Combo_worksheetLinkList, 497, 0, MSForms, ComboBox4cmd_calc5_ClearValues, 11, 1, MSForms, CommandButton?tc0_cmd_M5_calc1_showHideGuide, 1322, 2, MSForms, CommandButton??ME?????????????????????????????????????????????????????????????????????????????????????????????????????????????????????????????????????????????PSL????S????S?????s????s????<??<????? 4(8?????o??0?@?& ]????????XE? 'V?BstrMsg = "Selected worksheet: " & Me.Combo_worksheetLinkList.Value?3MsgBox strMsg, vbOKOnly, "Next Worksheet Selection"?'V 2 .B@0? 4(6? 4(8? ??!<!>$:(@ ??!<!>$:B@H?Sheets(Me.Name).Visible = False? 4(8? 4(6 2 .B@B?d'V?D |???&? ?0Error. Combo_worksheetLinkList_Change. in sheet: ??!? . at step= V F?Err No.= H!J?.  H!L'( ( P?ErrorA@N?D`o??X???&H]? ?8? 'V? 4(8? 4(6 2 ~B@0?7:41$X!Z!\?4:35$X!Z(\?=Rows("50").EntireRow.Hidden = Not Rows("50").EntireRow.Hidden?CRows("52:53").EntireRow.Hidden = Not Rows("52:53").EntireRow.Hidden?CRows("55:57").EntireRow.Hidden = Not Rows("55:57").EntireRow.Hidden?d'V? 4(8? 4(6 2 ~B@B?D?|????&?? ?=Error. tc0_cmd_M5a_calc1_showHideCalcDetails_Click. in sheet: ??!? . at step= V F?Err No.= H!J?.  H!L'( ( P?ErrorA@N?D?o????????????Z?Attribute VB_Name = "She@et8" ?Bast0{000?20820- C$0046}|Global!?Spac?False dCreatablPre declaId?TruBExposeTemplateDeriv$?Bustom izD2Control??Comb?o_works??LinkList, 497, 0, MSForm?s, ?Box?&cmd_calc5_Clear Value?11 , ?$mand@Button'tHc0_)M5?*1_showHideGu?)322?, ?V P@J?@L Sub ?'?*ick()  Application.En?PEventsK[A ? Range("C39:C?40").Br???G2= t10'? ?A?e0lect????: ?" & Me.?1K@???', vbOKOnly, "Next W?ŧ S?gJX???d2dAct`ebook.Unp?rot@ (g`z?@J??_passd@*? 6Scre enUpd@Bngϫ@;nE’s(?!`H?isiC??C?"O?).?#!'??) ?8???"?+.P3?- 710$7? Pexit?Z:E???e?]?gQBb.??O??g. in b?:?T?$ V". abt Qep=?I_ CA1&?SCrLf?! No.?`?.NumbercaaDescri?pቃW]?or?Z?z$ 4?;?G??????#$k?xF?K?F??FBV?t1cRow?s("4:35?W@Entire .Pbden?:NotB 37:41?n?c'35A\_@U?p;2:53?%?5Oid?5:?57??O?&?P??m?m>!p>2??U{O>tMUCUO=t-O= ap"?1. /aL?C??Det?ails?/>>>? ?;vb>&?v>?rr.>sg?l?l>> 2 ?>????l ?D??W??c??????????????????????????x=tc0_cmd_m9a_showHideCalcDetails, 2, 1, MSForms, CommandButton;tc0_cmd_m9a_calc1_clearValues, 3, 2, MSForms, CommandButton,CommandButton1, 4, 3, MSForms, CommandButton4cmd_Number_Sets_Select, 5, 4, MSForms, CommandButton2Combo_worksheetLinkList, 283, 5, MSForms, ComboBox??ME??????????????????????????????????????????? ????????????????????????????????????????????????????????????????????????????????????????????????PSL????S????S?????'??MsgBox num_selection?&?? ?0Error. Combo_worksheetLinkList_Change. in sheet: ??!? . at step= V F?Err No.= H!J?.  H!L'( ( P?ErrorA@N?D?o??????&?]????? 'V? 4(8?I@?4M9a_calc1_MDI_PMDI_ratio_in_the_isocyanate_feedstock$^(>?Y@?M9a_calc1_Cform$^(>???@?M9a_calc1_vair_input$^(>?ft3?M9a_calc1_vair_input_units$^(>????M9a_calc1_number_of_containers$^(>?Q@?M9a_calc1_Process_Temperature$^(>?F?#M9a_calc1_Process_Temperature_units$^(>?Expected result: 2.38E-05?M9a_calc1_expectedResult$^(>? 4(8?d'V?D?|????&?? ?5Error. tc0_cmd_M9a_calc1_checkValues_Click. in sheet: ??!? . at step= V F?Err No.= H!J?.  H!L'( ( P?ErrorA@N?Do??? ???&? ]?0?H? 'V? 4(8? 4(6 2 ~B@0?8:30$X!Z!\?8:30$X!Z(\?> Rows("40").EntireRow.Hidden = Not Rows("40").EntireRow.Hidden?CRows("42:45").EntireRow.Hidden = Not Rows("42:45").EntireRow.Hidden?d'V 2 ~B@B? 4(8? 4(6?D? |??? ?&? ? ?7Error. tc0_cmd_M9a_showHideCalcDetails_Click. in sheet: ??!? . at step= V F?Err No.= H!J?.  H!L'( ( P?ErrorA@N?D? o??? ?`?&? ]????? 'V? 4(8??C36:C39$^(>?Q@?C41$^(>?ft3?d38$^(>?F?d41$^(>??C50$^(>??C51$^(>??c52$^(>?ft3?d52$^(>??C53$^(>?Q@?C55$^(>?F?d55$^(>??C64$^(>??C65$^(>??c66$^(>?ft3?d66$^(>??C67$^(>?Q@?C69$^(>?F?d69$^(>??C78$^(>??C79$^(>??c80$^(>?ft3?d80$^(>??C81$^(>?Q@?C83$^(>?F?d83$^(>??C92$^(>??C93$^(>??c94$^(>?ft3?d94$^(>??C95$^(>?Q@?C97$^(>?F?d97$^(>??C106$^(>??C107$^(>??c108$^(>?ft3?d108$^(>??C109$^(>?Q@?C111$^(>?F?d111$^(>??C120$^(>??C121$^(>??c122$^(>?ft3?d122$^(>??C123$^(>?Q@?C125$^(>?F?d125$^(>??C134$^(>??C135$^(>??c136$^(>?ft3?d136$^(>??C137$^(>?Q@?C139$^(>?F?d139$^(>??C148$^(>??C149$^(>??c150$^(>?ft3?d150$^(>??C151$^(>?Q@?C153$^(>?F?d153$^(>??C162$^(>??C163$^(>??c164$^(>?ft3?d164$^(>??C165$^(>?Q@?C167$^(>?F?d167$^(>? 4(8?d'V?D`|??X?&P? ?5Error. tc0_cmd_M9a_calc1_clearValues_Click. in sheet: ??!? . at step= V F?Err No.= H!J?.  H!L'( ( P?ErrorA@N?D?o??????&?]??(? 'V?& Dim step As Integer, strMsg As String]???@?x??]??]??]??? 'V?A7'?? 4(8? 4(6? 'V? rndxMax = 10? Application.EnableEvents = False? ~.z?M9a_num_selection z%^!>'?? step = 10?'??40:40?+??42:45?+??54:54?+??56:59?+??68:68?+??70:73?+??82:82?+??84:87?+??96:96? +??98:101? +??110:110? +??112:115? +??124:124?+??126:129?+??138:138?+??140:143?+??152:152?+??154:157?+??166:166?+??168:171?+??'V 2 ~B@0? ??? ????&+ 1 ?$?$X!Z!\ ?$?$X!Z(\??? 2 ~B@B?Z'V ?$^B@H?d'V? 4(8? 4(6?Dx|??p?&h? 4(6? 4(8? ?7Error. tc0_cmd_M9a_showHideCalcDetails_Click. in sheet: ??!? . at step= V F?Err No.= H!J?.  H!L'(????? strMsg = "Error. cmd_calc1_showHideCalc_Click. at step=" & step ' & vbCrLf & "Err no=" & Err.Number & ". " & Err.Description ( P?ErrorA@N?D??&?o??????????????Attribute VB_Name = "She?et18" ?Basx0{00?020820- C$0046}|GlobaBl?Spac?False dCre atablPr@edeclaI"d?TruBExposeTemplateDer iv$?BustomizD2Control?tc0_cmd_m9a_showHideCalcDetails, 2, 1, MSFormCommandButton ???+c?'1_clearValue=#3,?*?>K4, @? ??? ,C Dim?As Int?eger,? @Str`v, lngRCLong??C ?hFO'?/?Ued ?:?$Me.?.ValuD?'?&?h Wo?rc ? ?$)?2$b Cb?boo?k.Unp?bR??O8R???rs(? )?.Visi`p?j? "( ?'?Name) ?8?l?Ht?Hq%%?s?B_D_Dj -=?5.?3:3.? in ?4:$:(@ ??!<!>$:B@H?Sheets(Me.Name).Visible = False? 4(8? 4(6 2 .B@B?d'V?D?|????&?? ?0Error. Combo_worksheetLinkList_Change. in sheet: ??!? . at step= V F?Err No.= H!J?.  H!L'( ( P?ErrorA@N?D8o??0??]?? ' $:B@Ho????]? ' $:B@Ho????0?&?]?p??? 'V? 4(8???@?m10_calc1_Vair$^(>?Q@?m10_calc1_Spray_Temperature$^(>?F?!m10_calc1_Spray_Temperature_units$^(>?2?m10_calc1_Percentage_MDI$^(>?@?@?m10_calc1_tsp$^(>?Expected result: 1.50E+00?m10_calc1_expectedResult$^(>? 4(8?d'V?D@|??8?&0? ?5Error. tc0_cmd_m10_calc1_checkValues_Click. in sheet: ??!? . at step= V F?Err No.= H!J?.  H!L'( ( P?ErrorA@N?Dxo??p???&`]????? 'V? 4(8? 4(6 2 ~B@0?7:27$X!Z!\?7:27$X!Z(\?> Rows("35").EntireRow.Hidden = Not Rows("35").EntireRow.Hidden?CRows("38:41").EntireRow.Hidden = Not Rows("38:41").EntireRow.Hidden)? a????? ?8?ޫ??c??????????????????????????x3Combo_worksheetLinkList, 1687, 0, MSForms, ComboBox;tc0_cmd_M8_calc1_ShowGuide, 368, 1, MSForms, CommandButton2#ListBox1, 3197, 2, MSForms, ListBox=tc0_cmd_M8_calc1_clearValues, 370, 3, MSForms, CommandButton27cmd_Number_Sets_Select, 371, 4, MSForms, CommandButton2&Spray, 3204, 6, MSForms, CommandButton??ME????????????????????????????????????????????? ????????????????????????????????????????????????????????????????????????????????????????????????PSL????S????S??????? ????? ? ????"?? ????? ?????? ?????0? ????????@???x?]?@]?X]?p]??]????,]?? ???? ??? ?@?x??tto]????num_selection =]??? 'V? ~.z? 4(6? 4(8?$X!Z!\'??MsgBox Is_hidden?M9_num_selection z%^!>'??MsgBox num_selection?step = 9? rfocus = "A7"?" Application.EnableEvents = False?# ?d'V 2 ~B@B? 4(8? 4(6?D|???&? ?=Error. tc0_cmd_m10_calc1_showHideCalcDetails_Click. in sheet: ??!? . at step= V F?Err No.= H!J?.  H!L'( ( P?ErrorA@N?D@o??8??&(]?P?h? 'V? 4(8??0C33, C40, C47, C54, C61, C68, C75, C82, C89, C96$^(>?A?0C34, C41, C48, C55, C62, C69, C76, C83, C90, C97$^(>?33333?X@?0C35, C42, C49, C56, C63, C70, C77, C84, C91, C98$^(>? 4(8?d'V?D |?? ?&? ? ?4Error. tc0_cmd_M9_calc1_clearValues_Click. in sheet: ??!? . at step= V F?Err No.= H!J?.  H!L'( ( P?ErrorA@N?D@ o??8 ??]????]?? ???(?@]?X]?p]??? 'V?A7'?? 4(8? 4(6? 'V? rndxMax = 10? Application.EnableEvents = False? ~.z?m9_num_selection z%^!>'?? step = 10?'??35:35?+??42:42?+??49:49?+??56:56?+??63:63?+??70:70?+??77:77?+??84:84?+??91:91? +??98:98? +?? rndxAry(11) = "100:100"? rndxAry(12) = "103:106"?rndxAry(13) = "113:113"?rndxAry(14) = "116:119"?rndxAry(15) = "126:126"?rndxAry(16) = "129:132"? rndxAry(17) = "139:139"?rndxAry(18) = "142:145"?rndxAry(19) = "152:152"?rndxAry(20) = "155:158"?'V 2 ~B@0? ??? ???"* 2 + 1 ?$?$X!Z!\ ?$?$X!Z(\??p 2 ~B@B?Z'V ?$^B@H?d'V? 4(8? 4(6?D|???&? 4(6? 4(8??-Error. cmd_calc1_showHideCalc_Click. at step= V F?Err no= H!J?.  H!L'( ( P?ErrorA@N?DP?&Ho??@?8Private Sub tc0_cmd_M8_calc1_showHideCalcDetails_Click()?End Sub?? ??! ??!<(>o????????????k?Attribute VB_Name = "She?et35" ?Basx0{00?020820- C$0046}|GlobaBl?Spac?False dCre atablPr@edeclaI"d?TruBExposeTemplateDer iv$?BustomizD2Control?Combo_works?LinkList, 1687, 0, MSFo rms, Box???&tc0_cmd_M8_calc1_ShowGuide, 3 68?*?'mand?Button2?*KH?;1?!19J2"??$clear Value537?83q%?9Numb?er_SetsHlecN37*4A????       ????    !               " # $ % & ' ( ) * + , - . / 0 1 2 ????4 5 6 7 8 o w ; = ? > ? @ A K C D E F G H I J : L M N O P Q R S T U V W X Y Z [ \ ] ^ _ ` a b c d e f g h i j k l m n ????p q r x t u v ????? ? ????{ | } ~  ? qSpray920?6U?:Option ??lic?it P@?A@? Sub S&_C k() Dim row_num As In teger?validN@ _se?8??col_f?or?S??ngstep?, s`trMsg?? rndxAry(12)?Varia?n@T?23A?D, AMaxh#Is_hiddDen!Boo@CnX '@?=?w?s?W?e/ ??= 9 a ??B = Ac?t?u??App`1a?8.Scree?nUpd?ng@rMDz ?En?yE?vents?c '= Rows(8).Entire٠.H?#'@/?if &? L?.Range("M?9?E??").h?$?? j?"' #?"'` rfocu!"A~7@Y ?&@??'? ??'?d10???A= 2?'??? ?V) 2?"32:38D%? Y`?39:4!?A?%3b46:5A?)4"53:59? 5"60:66?,6#7:73,?7"74:80,?8"81:81eB9#8:94l10B95:101?dc!?'If?J?"?? The?jA??? ?y? 35:??&'u@*2(#'48:5? ?D2:4??h?61:6? ?,d?'vC??7 2(4??gqt7:9<d3:6??100?2( 0:7??c113:1?1U ??`!?3@126:12?&2?(D`#% ?c 1`-1%?O?#$91:9???152:?15|1@!$&?'?4??2?16(6?C??b%?54ed ?b'?8:4o ?!59~7?3?(51:5?=!372:7?<3(as64:6O8(5:8|3$'77??;=4?v?90$:9/'11B11^1?#e??0P%0?[%#124?#_30)?O61? 1?37:0?E3d'?(W??m15 35?u1?Cp):16W? ??6??8??85?%?5?%CR??edC?~.UnprotQ ? (g??_?_?passжd`?Q?@S?w10nS`??Q`U?1 To ,w???? (q)O??(?Q??[e?}2?Ӆ???? }?3oo?E??C E nd If?Ne?x???????????ГD?Ho????!?= ???/?'??m??+ ?1????ɣ1 ??s??y%??';oo???CG z? 'If num_selection = ?10 Then?do nothi?ng@Else( For rndxr ?+ 1 To?NRows(PAry)).@Entire. Hidde}Tr?u^Next:?End If!?step~90 Range("M9_ ?").SO??#10?#A??veSheet .Prot?? (@glob_s? _password) %Applica??oableE?vents?Om ScreenUp2d?ng ?+ exit_sub : E Sub9 rr? ?- EnA?)strMs?$"Error. cmd_calc1I?@owmeC@_C?? C&1X52:`c ?2?`??&155??&e?dO%M?\.Unprot?? (glob_B?_pass0word ?!mFofr?:?Q1 ???b'?* 2 + 1?;??Rows(?-??))`?tire ".??den` Nodt _en ?N?ext#?Pr~d 9?m?xC?).S??? ??`L?????c?xt3ie?x??Q?? G~}1}?}?n}{s?&?v?y{noo{?o{?o{ o{ l{ On~ P??(???X}? '?}???}lc?}? '???r_?'p???0?Combo_P3?tLinkLxist??d????` ???x?]?@]?X]?p]??]???? ]?? ???? ??? ?@?? ?x?f, rndxAry5(12) As Variant]????]????num_selection =]??? 'V? ~.z? 4(6? 4(8?$X!Z!\'??MsgBox Is_hidden?M9b_num_selection z%^!>'??MsgBox num_selection? 'V?'?? Application.EnableEvents = False?46:69?+??70:93?+??94:117?+???118:141?+??142:165?+??166:189?+??190:213?+??214:237?+??238:261? +??262:285? +??If Is_hidden = True Then?51:51?+??75:75?+??99:99?+??123:123?+??147:147?+??171:171?+??195:195?+??219:219?+??243:243? +??267:267? +??53:54?+??77:78?+??101:102?+??125:126?+??149:150?+??173:174?+??197:198?+??221:222?+??245:246? +??269:270? +??59:66?+??83:90?+??107:114?+??131:138?+??155:162?+??179:186?+??203:210?+??227:234?+??251:258? +??275:282? +??'V 2 ~B@0 ?? ?? ??? ??? ?$?$X!Z(\ ???? ?$?$X!Z(\? ?$?$X!Z(\? ?$?$X!Z(\?,Rows(rndxAry5(rndx)).EntireRow.Hidden = Trued??Pk??H??@?? $?$X!Z(\ ????? $?$X!Z(\?? $?$X!Z(\?? $?$X!Z(\?+R'ows(rndxAry5(10)).EntireRow.Hidden = Trued??pk??hd??`? ??? ?? ?? ?$?$X!Z(\ ???? ?$?$X!Z(\?? ?$?$X!Z(\? ?$?$X!Z(\?,Rows(rndxAry5(rndx)).EntireRow.Hidden = Trued??xk??p??h?If num_selection = 10 Then? do nothing?Else? ?? ?? ? ?? ?$?$X!Z(\???k????Z'V?M9b_num_selection$^B@H?d'V 2 ~B@B? 4(8? 4(6?Dp|??h?&`? 4(6? 4(8??-Error. cmd_calc1_showHideCalc_Click. at step= V F?Err no= H!J?.  H!L'( ( P?ErrorA@N?D?o?????&?]?X?p????? 'V?BstrMsg = "Selected worksheet: " & Me.Combo_worksheetLinkList.Value?3MsgBox strMsg, vbOKOnly, "Next Worksheet Selection"?'V 2 .B@0? 4(6? 4(8? ??!<!>$:(@ ??!<!>$:B@H?Sheets(Me.Name).Visible = False? 4(8? 4(6 2 .B@B?d'V?D|???&? ?0Error. Combo_worksheetLinkList_Change. in sheet: ??!? . at step= V F?Err No.= H!J?.  H!L'( ( P?ErrorA@N?DPo??H???&8]???? 'V? 4(8???@?M9b_calc1_Aspray$^(>?(@?M9b_calc1_Duration_of_spray$^(>?4@?M9b_calc1_Airflow_Speed$^(>?miles/hr?M9b_calc1_Airflow_Speed_units$^(>??R@?%M9b_calc1_Temperature_of_Process_Area$^(>?F?+M9b_calc1_Temperature_of_Process_Area_units$^(>?I@?M9b_calc1_Percentage_MDI$^(>?ERange("M9b_calc1_expectedResult").Value = "Expected result: 8.38E-04"? 4(8?d'V?D(|?? ?&? ?5Error. tc0_cmd_M9b_calc1_checkValues_Click. in sheet: ??!? . at step= V F?Err No.= H!J?.  H!L'( ( P?ErrorA@N?D`o??X?(?&H]?h??]????????]?]?]? U???? g@?ޛC??c??????????????????????????xCtc0_cmd_M9b_calc1_showHideCalcDetails, 2, 1, MSForms, CommandButton;tc0_cmd_m9b_calc1_clearValues, 3, 2, MSForms, CommandButton=tc0_cmd_M9b_calc1_showHideGuide, 4, 3, MSForms, CommandButton4cmd_Number_Sets_Select, 5, 4, MSForms, CommandButton2Combo_worksheetLinkList, 441, 5, MSForms, ComboBox??ME??????????????????????????????????????????? ????????????????????????????????????????????????????????????????????????????????????????????????PSL????S????S???????@??08? Lh? ????? ??????????????????? ????? ????"????? ??????? ??????? ??????? ????????? ????? ????? ????? ?????? ????? ? ????? ????? ? (? ?????8? ????? @? &X? ????? ??(?? ????? ????? ????? ???? ????? ????? ????? ?? ????? ???????? ?8?P?h??????????????(?@?X?p?????????????0?H?`?x????? ????? ????? ????? ?????????"??2? ?????8?@?P?X? ?????h? ????? p? ???????? ?? ??t??@?X? ?????`"?h?p?x??? ?? ???? ?????.?? D?? J8? J???? ?? ??? ????? ????? ??????? ??(??????? ????"??????? ? ????? 4(? ?????`??????????? ??????0?P?h????? ???????????0?P? ?????p?????????? ????? ?@?`?x????? ??????????(?@?`? ???????????????? ?????0?P?p??????? ???????? ?8?P?p? ?????????????? ? ????? @?P?X?`?h??p? ? ?( ? ????? ????"?0 ?8 ? ?????P ? ????????0? 'V?A7'?? 4(8? 4(6? 'V? rndxMax = 10? Application.EnableEvents = False? ~.z?M9b_num_selection z%^!>'?? step = 10?'??If Is_hidden = True Then?51:51?+??53:54?+??59:66?+??75:75?+??77:78?+??83:90?+??99:99?+??101:102?+??107:114? +??123:123? +??125:126? +??131:138? +??147:147?+??149:150?+??155:162?+??171:171?+??173:174?+??179:186?+??195:195?+??197:198?+??203:210?+??219:219?+??221:222?+??227:234?+??243:243?+??245:246?+??251:258?+??267:267?+??269:270?+??275:282?+??'V 2 ~B@0? ??? ????&+ 1 ?$?$X!Z!\ ?$?$X!Z(\??? 2 ~B@B?Z'V ?$^B@H?d'V? 4(8? 4(6?Dh |??` ?&X ? 4(6? 4(8??-Error. cmd_calc1_showHideCalc_Click. at step= V F?Err no= H!J?.  H!L'( ( P?ErrorA@N?D? o??? ?P?&? ]????? 'V? 4(8? 4(6 2 ~B@0?7:41$X!Z!\?7:41$X!Z(\?=Rows("50").EntireRow.Hidden = Not Rows("50").EntireRow.Hidden?CRows("52:53").EntireRow.Hidden = Not Rows("52:53").EntireRow.Hidden?CRows("55:57").EntireRow.Hidden = Not Rows("55:57").EntireRow.Hidden?d'V? 4(8? 4(6 2 ~B@B?D?|????&?? ?=Error. tc0_cmd_M9b_calc1_showHideCalcDetails_Click. in sheet: ??!? . at step= V F?Err No.= H!J?.  H!L'( ( P?ErrorA@N?Do?????&]??? 'V? 4(8?. Range("M9b_calc1_expectedResult").Value = " "??c47:C50$^(>?ft/sec?d50$^(>?D?c52$^(>?F?d52$^(>??c55:C57$^(>???????@?c58$^(>??c71:C74$^(>?ft/sec?d74$^(>?D?c76$^(>?F?d76$^(>??c79:C81$^(>???????@?c82$^(>??C95:C98$^(>?ft/sec?D98$^(>?D?C100$^(>?F?D100$^(>?? C103:C105$^(>???????@?C106$^(>?? C119:C122$^(>?ft/sec?d122$^(>?D?c124$^(>?F?d124$^(>?? c127:C129$^(>???????@?c130$^(>?? c143:C146$^(>?ft/sec?d146$^(>?D?c148$^(>?F?d148$^(>?? c151:C153$^(>???????@?c154$^(>?? c167:C170$^(>?ft/sec?d170$^(>?D?c172$^(>?F?d172$^(>?? c175:C177$^(>???????@?c178$^(>?? C191:C194$^(>?ft/sec?d194$^(>?D?c196$^(>?F?d196$^(>?? c199:C201$^(>???????@?c202$^(>?? c215:C218$^(>?ft/sec?d218$^(>?D?c220$^(>?F?d220$^(>?? c223:C225$^(>???????@?c226$^(>?? c239:C242$^(>?ft/sec?d242$^(>?D?c244$^(>?F?d244$^(>?? c247:C249$^(>???????@?c250$^(>?? c263:C266$^(>?ft/sec?d266$^(>?D?c268$^(>?F?d268$^(>?? c271:C273$^(>???????@?c274$^(>? 4(8?d'V?D?|????&?? ?5Error. tc0_cmd_M9b_calc1_clearValues_Click. in sheet: ??!? . at step= V F?Err No.= H!J?.  H!L'( ( P?ErrorA@N?D?o????0 ??! ??!<(>o????????????"?Attribute VB_Name = "She?et28" ?Basx0{00?020820- C$0046}|GlobaBl?Spac?False dCre atablPr@edeclaI"d?TruBExposeTemplateDer iv$?BustomizD2Control?tc0_cmd_M9b_calc1_showHideC?Details, 2, 1, @MSFormCommandBu?tton???.m?.clearValtue#3,?*?YG?u., 4, ???ANumber _Setsle?ct, 5B?Ibo_works??LinkLis9?44?RIboBox@ROption ??lici?t P{} Sub ?(_C k() Dim row_num As Integer?val?idN@ _se;??col_fo?r_?S??ngstep?, s`trMsg?? rndxAry(12)?VariaVn?B?234?  ', ? 5L? AD"?MaxhIs_hid?den!BooV?n '@?$=?4ws?W?<6 ?"= 9 a??J = Act xb??App`8a??.Scre enUpd?ng??t?| ?EnA|?Events?c '= Rows(7).Entir?e?.`|?#'@6??O &? L?.Range("?o?").?z%? ??#? A?$10??a8?2= 2?'_? ? dA(1)? #"46:69?k% Q??70:9 3,3b94:117L4B118P:141l5c4?2:165l6c?66:187c?90:21M8b@214:23m9Ac38:26m1?0?62:28??##?'If?=@$??? The@]?$?D%C?s? 51:5 2"(?(5:7l2(??(9:9L2(?( 23:12l2(M)7?,?2($)701:17??5:?19??9p ?`43:24 ?7? n?Jc3:5?4?3e7:7??K??3d100?2}?26???9:150?? n7?? 9 ?2?1:22 ?5?? ?07 ??$?[Qs9:64t8h3:9 4v0 1U 4%3@3 4?%5@6 4%@?8?s20`!1 ;uP!3 t0325? u7P8 0ctQ?OCc.Unp?rot?? (gp??? ?_pass??~dP??%cP>ZX?>10~>P??s? To^ ?[??c$+(q)߿d??jQOFe?}~2?Cj?S?]3?__?9 4__R?'i5oobE???@End If?3Nexp?????(?!?????\0?noA?4?L??@?= ?B???=??? 'R'???__ ??,?m??+ 1?v??-????-s%?-?????Q//?#?-??a' ??????-A??G?'da?Fothi?ġ '?r?I?P? To 10  Rows(r@ndxAry8)).Entired.Hidden? = True?0Next Enpd If"?shtept9?4Range("M9b_num_selection"x).S A G1 0HA0veSheet.Prot@ (glob_s_password) JApp0licaj?ableEvents?m Screen?Upd?ng ?+ exit_s(ub: E S?ub rr? ?- En?SstrMs?I"Error. cmd_cal$c1?ow??eC ?_Cyk. a?t ??=" & _?*i& vb0CrLf? no? ?.Numbder. ??D?escrip?Q???!Box?A$,OKOnly, e?&"C Go??J ???H PrivateAL CoPmbo_?nkrLinkList_?Ch??sOn @!8or X?Dim7As Int?eger,?% ?String, lngRCLo??@R????EC????'^?ed ?+":IMe.?1.V4al?'?M?? W?or?@ ?ȃ O?(2J?book0.Unp??zSFa|lsd?S?C?ss(?!).Visi_?q*l??)k?'?N?ame) ?8G???؁?&._? #$?K$7_???gQBb.?g.? in ?j:?y?2??$?{??No.??g?????? !??t8c0_?A?c?ch?eckBsC?(_???/Y?l4??FNL(???Aspray?Bc?] ?00## ?D?ur??_of_2?Airflo?w_SpeedH2? _unitsx"miles/hr?\n Tem?pe? ure? ?/cess_Are?ah75 C???F_SPerc?|age_MDI?5u'? exp??edResul?t8"E? r?: 8.38E-?04?? ?zS9>???t3.e??~=//?=??=Q?????=??s??o ??=?=sh?Detail?/>߀ V????g?#Srnd°30)q?Varianxt, qƅM ax8?focu~s酧?~?w??e?[??_?&9?r= "A7??+??L6??LY^p^O?D???'??=v?'??u?Setr ?= ؿ? K=?P.?>?E>?_??"?? = 3:z?%'If Is_?h?? Then?'??1)?_"5?1:514E?2?X3:5?F?3?9(:66<4?75(:75?5?7:78?6?83:90?7?99:99?8?101P:102?9?7h:11? 1?4(1X23:0?1?1,25??1?13? 3- 1140:4?- ?&C14P9:15-1s1*506? 1?17?07?1?17? ?7~708? ?909}29? 9}2203:21? 2219 ?2221:22w4?dxAry(24) = "227:234" )rn?5p43P:243p6858687851:?2588886s6799:2?70 307s?82? ? C step?20ActiveSheet.Unprotect ?(glob_s? _passwor?d)For ??!1 To nu m_sel?ion * 3 '+ 1?ERows(??)).E ntire? .H idden?%Not !,?Nexft??bPr?a??9??Range(rfocus).S?3?C? 10? CApplicat?=4ableEvents3True ScreenHUpd? ng? exit_sub:C E? Sub? err??T?[Ab%strMsA "Error. cmd_calc1I?|oweeC@_C8k. at !?@=" & _?*?& vbCr?Lf? no? ?.Number. ??DespcripM??!B,ox?A$,OK?Only, ?&ķGo@?J EndJPrivate tc0_A3M9bL4Guide?4(??On $?Yc c-C Dim?As IntePger,$ @S?tringCFC?!?/Fals?B= ?sks??h"7:?41"[mu?'?50?2k2:53??+ 5:57?> ?# F6?y?f?\???o(6?????}?!n?wW^?xDetaiDlseyin º:!rMe.Name?Ct?|?|No.?|?|?|| [|cle?arValue??||?"??"F_?;?' se"?HexppredResul?t`,2 ?`" ?NS??c47:C?5u $+?d?"ft/?sec?%52h?68?d?"F??5??6??r"c@??).?7.2??c71:C74( ? e("c766 ?d? 79?:C8QP  ? ?T9C9P98 ??D?  C??/ ?% D?= ?3:@?5 10???C11?12? ???? ?12??$???1?C129? ? c13?f/%?F?C149? ?? }? 49? ?? 0?C?1"m?%?%15???CпC1?G(? ??? ? 7/> 21?? `? _>c17G?? ? C19p>1?99? ?? ? 9I?>?? 9.20?>9? 20?? 221??>219? ?? ? <22?,? ?? 22??22?? 2?? ?? 349? ?? }? 4I? ?? l2?4?? *l? ? 6?69? ?? ? 6I? ?? Range("d268").Value =? "F" ?xc271:C27*3?0?487.2< Application.EnableE ventslTr?ue$step10[exit_Psub:E Sub err?strMsg4"Error. tc0_cmd_M9b_calc?1_clear?s_C?k. in sheet:" & Me.Name?". a?t ?B= G_???& vbCrL?f??6 No.??.Number?!?? Descrip?y"?TBox 0?Y,?&OKOn0ly, ^??GoTo  End| Pr ivate Work?b_Act  ()?3e.Co mbo_wLi?nkList??z???????????????????????x3Combo_worksheetLinkList, 1260, 1, MSForms, ComboBox??ME???????????????????????????????????????????????????????????????????????????????????????????????????????????????????????????????????????????????(SL????S????S?????s??????N0{00020820-0000-0000-C000-000000000046}????` $?????????????????????????????!!?`?V??????????`?(??????????`?*??????????x`?,?????????? R?????????????????????????????????????????????????????% %*?=???????????????????????????????????????????????????????????????????????????????????????????????????????????@?`?X*\R8004*#63???(?? ????"???? ?????8? H@? :?? ????????? ?? ?? ??????? &0? ????? X? h?x? ??????? ????? ??????????????8?P?X? ????? ????"?`?h? ??????? ????????????x??&h]?@?X?p????? 'V?BstrMsg = "Selected worksheet: " & Me.Combo_worksheetLinkList.Value?3MsgBox strMsg, vbOKOnly, "Next Worksheet Selection"?'V 2 .B@0? 4(6? 4(8? ??!<!>$:(@ ??!<!>$:B@H?Sheets(Me.Name).Visible = False? 4(8? 4(6 2 .B@B?d'V?Dh|??`?&X? ?0Error. Combo_worksheetLinkList_Change. in sheet: ??!? . at step= V F?Err No.= H!J?.  H!L'( ( P?ErrorA@N?D?o????? ??! ??!<(>o??x????p?????Attribute VB_Name = "She?et31" ?Basx0{00?020820- C$0046}|GlobaBl?Spac?False dCre atablPr@edeclaI"d?TruBExposeTemplateDer iv$?BustomizD2Control?Combo_works?LinkLis?t, 1260?, MSForm?s, Box???Option Vlicit PIM Sub?*_Chang@e() Orror GoTo err_sub Dim step As Integer,?rMsg S??ng, lngRCLo?str?????C= t10?'? ???e0lectS?@: ?" & Me.?F?.Val?mA'@?D?', vbOKOnly, "N ext WV S/?@M?O?%2?%Actvbook.@Unprot?' (g?_?h_pa4ss+d?QAp paad.Scr@eenUpd?nNg?wć? En?E?ventsK ?G?s(?@).Vis?iû??&?DDdG?A?I?0? I<,??"??+.P?-cJ$7?@ exitaY:?E?Abc\??O E?`.\f. in: ??:dS?$?T".? at?Oep=-?_CA1&RCr Lf! No.?`.NumbercaaDesc??,?? V?`?p??? ?? ???? ?? "???? ????? ??????? ???????8? X? ?????x??? ?? ??????? B?? |? ????? B??&?? ????? 4? $8? (`??????????? ?????4?@? ?????P?X??`? H? ?????H?P? ?????X?`?h?p?v??? ????? ?(?????????????????????????????????????????????????????????????????????????????????????????????????????????????????????????????????????????????????? ????? ????B? 0?8?@? DX?:?? ???????????? ???????0& ? ?????P?`?h? ?????????/?? ??????? ??????? J??8?/ ?;8?/P?h? ????? ?????p?x? ???????????4??ry??.H? ?????`?h? ????"? p? x? ??????? ????"? ?? ?? ??????? ?? ?? "?? ? "0? X? .x? ?? ?? ????? ?? ?? $? 8? &P? &x? .?? .?? ? 0? 8? P? ????? "`? ?? "?? ?? .?? ? (? <0? p? x? &?? &?? .?? .? @? 0H? x? ?? ????? ?? ?? 0?? ?? @?? 48? 8p? ?? ?? ?? ????"? ??????? ????? Z?Np? T??F?`? ????"?  h? p? ?? ?????? ????B?  ?????? ????"?  ?? ???? ? ? ? ????B? ?0 ?8 ?P ?h ?x ?? ?? ? ????? ????? ????? ????? :? ? !? ????? !? ?????@!? >H!??!??!???!? ?????H"?P"?X"?p"???"? #?(#? ????? V0#? <?#? ?#? ?#? $? $? @$? X$? 4h$? H?$? ?$? ????? ????? ?$? ????? ?????%?%? ????? ?????0%?P%? p%? ??????%??%??%? ??????%??%? &? ????? &? B(&? ????? ????? $p&? 0?&? 0?&? 2?&? 20'? ?????$?(?????N?????????????????????????????x??ME?????????????(???????????????????????????????????????????????????????????????????????????????????????????????????????????????????????????????0??^6 ?????????L????????????????L????????????<,??<0??<4??<8??<<??NOTE: temp and temp_rng must both be F or C, not mixed units.?2 get_adjustFactor = 0# 'no adjustment is default? step = 10?EDim temp_idx As Integer, temp_lower As Integer, temp_upper As Integer?UIf temp < WorksheetFunction.Min(temp_rng) Then temp = WorksheetFunction.Min(temp_rng)?UIf temp > WorksheetFunction.Max(temp_rng) Then temp = WorksheetFunction.Max(temp_rng)? step = 11?5temp_idx = WorksheetFunction.Match(temp, temp_rng, 1)?;temp_lower = WorksheetFunction.Index(temp_rng, temp_idx, 1)??temp_upper = WorksheetFunction.Index(temp_rng, temp_idx + 1, 1)? step = 20?KDim MdiPct_idx As Integer, mdiPct_lower As Integer, mdiPct_upper As Integer?]If MdiPct < WorksheetFunction.Min(mdiPct_rng) Then MdiPct = WorksheetFunction.Min(mdiPct_rng)?]If MdiPct > WorksheetFunction.Max(mdiPct_rng) Then MdiPct = WorksheetFunction.Max(mdiPct_rng)?;MdiPct_idx = WorksheetFunction.Match(MdiPct, mdiPct_rng, 1)?DmdiPct_lower = WorksheetFunction.Index(mdiPct_rng, 1, MdiPct_idx, 1)?HmdiPct_upper = WorksheetFunction.Index(mdiPct_rng, 1, MdiPct_idx + 1, 1)? step = 30?bDim af_minT_minM As Double, af_minT_maxM As Double, af_maxT_minM As Double, af_maxT_maxM As Double?Laf_minT_minM = WorksheetFunction.Index(adjFact_rng, temp_idx, MdiPct_idx, 1)?Paf_maxT_minM = WorksheetFunction.Index(adjFact_rng, temp_idx + 1, MdiPct_idx, 1)?Paf_minT_maxM = WorksheetFunction.Index(adjFact_rng, temp_idx, MdiPct_idx + 1, 1)?Taf_maxT_maxM = WorksheetFunction.Index(adjFact_rng, temp_idx + 1, MdiPct_idx + 1, 1)? step = 40?Finterpolate the pct MDI first, then interpolate for temp to get answer?2Dim af_minT_newM As Double, af_maxT_newM As Double?Dim result As Double?waf_minT_newM = ((MdiPct - mdiPct_lower) / (mdiPct_upper - mdiPct_lower)) * (af_minT_maxM - af_minT_minM) + af_minT_minM?waf_maxT_newM = ((MdiPct - mdiPct_lower) / (mdiPct_upper - mdiPct_lower)) * (af_maxT_maxM - af_maxT_minM) + af_maxT_minM?iresult = ((temp - temp_lower) / (temp_upper - temp_lower)) * (af_maxT_newM - af_minT_newM) + af_minT_newM? step = 50???????strMsg = af_minT_minM & "," & af_minT_maxM & ", " ' & af_maxT_minM & ", " & af_maxT_maxM & "; new: " ' & af_minT_newM & ", " & af_maxT_newM & " => " & result?DMsgBox strMsg, vbOKOnly, "minT-MinM, minT-MaxM,maxT-minM, maxT-maxT"? step = 100? get_adjustFactor = result? exit_sub:? Exit Function?err_sub:?0get_adjustFactor = 0# 'no adjustment is default?????strMsg = "Error. module1. get_adjustFactor. at step=" & step ' & vbCrLf & "Err No.=" & Err.Number & ". " & Err.Description?" MsgBox strMsg, vbOKOnly, "Error"? GoTo exit_sub? End Function? ??&0]????]?0?H?`]?x???9NOTE: temp range is limited from guidance doc 20C to 400C?ASSUMES temp units are C.?'? default? 'V?8check for out of range temp. set to max or min available   0%2   0%4??O use equation to calculate the vapor pressure. See guidance doc for reference.]???? ?? '6 6?????MbP? ??'8?'$d??P??Q??k$@?? 6 '8? 8 0%:????Q?~?'$k???<?k????'V  ? 0%>'&  &? 0%@'(  &? ? 0%@'*?'V " &? 0%@', " &? ? 0%@'.?('V?<interpolate the temperature to get answer for vapor pressure?uresult = ((temp - temp_lower) / (temp_upper - temp_lower)) * (vapor_pres_upper - vapor_pres_lower) + vapor_pres_lower?<interpolate the temperature to get answer for vapor pressure]?????? ?8?P?. result = ((1-0)/(5-0))*(0.0022-0.0012)+0.0012? result = (1/5)*(0.001)+0.0012?" result = (0.0002)+0.0012 = 0.0014? ?fffffq@ 'B? (?fffffq@ 'D? *?fffffq@ 'F ,$N'H .$N'J B D  F D  J H  H 'L L$P'$?2'V?<????????strMsg = temp_lower & "," & temp_upper & ", " ' & vapor_pres_lower & ", " & vapor_pres_upper & "; new vapor pres: " ' & result?BMsgBox strMsg, vbOKOnly, "T min,max to Vapor Pres min Mix, result"?d'V $'?D?z????&??'? default??0Error. module1. get_HgVaporPress_mmHg. at step= V F?Err No.= H!J?.  H!L'( ( P?ErrorA@N?D?i????h?&?]??(?@?>NOTE: temp and temp_rng must both be F or C, not mixed units.?4@'R?%default set to lowest value in table.? 'V V?C??'V T'$ V?Fe?'V?@?"@ T?@@ '$ V?Ke?('V T?fffffq@ '$d??x?2'V X 0%2'$k??P?<'V?Dcheck if temp in C is within range. if not set to either max or min. $ X 0%2 ? X 0%2'$ $ X 0%4 e X 0%4'$k????d'V $'R?Dxz??p?&h?9@'R?default is standard temp of 25C??+Error. module1. convert_temp_to_C. at step= V F?Err No.= H!J?.  H!L'( ( P?ErrorA@N?D? i??? ?X? 4(8o??p ??? 4(8o??P ?Sub AddNew_workbook()?Dim NewBook As Workbook?Set NewBook = Workbooks.Add? With NewBook? .Title = "All Sales"? .Subject = "Sales"?( .SaveAs Filename:="Allsales.xls"? End With?End Sub?Sub AddNew_worksheet()?Dim NewSheet As Worksheet?Set NewSheet = Worksheets.Add? With NewSheet? .Name = "new Worksheet"? '.CodeName = "sheet100"?( .Outline.ShowLevels(3, 3) = True?' .Outline.AutomaticStyles = True??) '.SaveAs Filename:="Allsales.xls"? End With?End Sub?Sub AddNew_worksheet_copy()?Dim wss As Worksheets?Dim NewSheet As Worksheet'''??'wss("sheet1").Copy after:=wss("sheet3")?Worksheets ("sheet1")??5Worksheets("Sheet1").Copy after:=Worksheets("Sheet3")?? With NewSheet? .Name = "new Worksheet"? '.CodeName = "sheet100"?( .Outline.ShowLevels(3, 3) = True?' .Outline.AutomaticStyles = True??) '.SaveAs Filename:="Allsales.xls"? End With?End Sub?Sub myOutlines()??)Worksheets("Sheet1").Outline.ShowLevels 2??:This example sets the outline level for row two on Sheet1.?-Worksheets("Sheet1").Rows(2).OutlineLevel = 1?2Worksheets("Sheet1").Range("3:4").OutlineLevel = 2???End Sub??]?MSForms - Copy.exd?]? MSForms.exd?0???STry to rename the C:\Users\[user.name]\AppData\Local\Temp\Excel8.0\MSForms.exd file?TEMP$f? \Excel8.0\ b?TEMP$f? \Excel8.0\ `A@d?NTry to rename the C:\Users\[user.name]\AppData\Local\Temp\VBE\MSForms.exd file?TEMP$f?\VBE\ b?TEMP$f?\VBE\ `A@do????H h$l? jA@n h j?k??Xo??P?? p$~?'li??(?( p$l? p tA@r pA@vk???o???? ???&?]?X?p??]??????]???]??0?H]?`?x??]???????4NOTE: temp range is limited from guidance doc to ????ASSUMES temp units are C.?'x? default? 'V?8check for out of range temp. set to max or min available   0%2 ??ċ???4?>'$?You have entered a very low temperature. The diffusivity in air calculation will assume a temperature of 10 degrees Fahrenheit. ??NoticeA@N?<?k???   0%4??????H?>'$??You have entered a very high temperature. The diffusivity in air calculation will assume a temperature of 130 degrees Fahrenheit. ??NoticeA@N?<?k????O use equation to calculate the vapor pressure. See guidance doc for reference.?6 Dim tempKel As Double ', dbl_logVaporPress As Double? tempKel = temp + 273.15? MsgBox tempKel? If tempConv < 0.001 Then? dbl_logVaporPress = 0? result = 0?Else? - dbl_logVaporPress = 10.21 - 2961 / tempConv? A result = WorksheetFunction.Power(10, dbl_logVaporPress) * 0.0075?End If? GoTo MsgOut?'V]????   ? 0%>'&  &? 0%@'(  &? ? 0%@'* ?fffffq@ '? (?fffffq@ '? *?fffffq@ '??'V z &? 0%@'| z &? ? 0%@'~?('V?<interpolate the temperature to get answer for vapor pressure?temp_inv = 1 / (temp + 273.15)?*temp_lower_inv = 1 / (temp_lower + 273.15)?*temp_upper_inv = 1 / (temp_upper + 273.15)?+vapor_pres_lower_ln = Log(vapor_pres_lower)?+vapor_pres_upper_ln = Log(vapor_pres_upper)?? result_ln = ((temp_inv - temp_lower_inv) / (temp_upper_inv - temp_lower_inv)) * (vapor_pres_upper_ln - vapor_pres_lower_ln) + vapor_pres_lower_ln?result = Exp(result_ln) ??ffffff?? 0%:'?? MsgBox temp_onepointnine ??ffffff?? 0%:'?? MsgBox temp_lower_onepointnine ??ffffff?? 0%:'?? MsgBox temp_upper_onepointnine ? ? '? ? ? '? ? ? '?? MsgBox temp_diff_lower ~ | '? ? ?'? ? ?'?? MsgBox diff_fordiff ~ ? '$?(result_onepointnine = (temp_onepointnine?uresult = ((temp - temp_lower) / (temp_upper - temp_lower)) * (vapor_pres_upper - vapor_pres_lower) + vapor_pres_lower?2'V?<????????strMsg = temp_lower & "," & temp_upper & ", " ' & vapor_pres_lower & ", " & vapor_pres_upper & "; new vapor pres: " ' & result?BMsgBox strMsg, vbOKOnly, "T min,max to Vapor Pres min Mix, result"?d'V $'x?D?z????&??'x? default??0Error. module1. get_diffusivity_m2sec. at step= V F?Err No.= H!J?.  H!L'( ( P?ErrorA@N?D?i????????????u?Attribute VB_Name = "Module1" Option Explicit ' global constants& ?PubL C0J_sheet_password As S?ng??PSRA?8>!Gcommoutilities and func+?h'eF gaadjustFactor(te$mpjDo?e,? MdiPct !_r??Ran?g_?A'?Emo /?-? )(\O?rror GoTo err_sub)Dim ste?IInteger,rMsg?!????>'NOT?E: ?`}Tmo both be F 4C, not mixed units."b????0# 'no ?ment is defXaul?u? B '!C*= 10? '?A/?!idx?+F0 lower?upNp??DIf8<` Work??s.Min?o?Z) Thhen? =? ?>?? ax?? ?DBr?G1??F?(atch,?1?5, 1)??PQInde??,D?aMC[i +? 1G?$2)?cg?_m??d????Dr5@?? td@?Q!F?d?`Ld5A t?R?An ?$? "$?"@?, ??h8??@j???O BV ?B3?Baf_?minT?M?e???ax?ax????D+? ?+d??id3?$A ?_ PG ?#? ??!?? ? I9?/'??? @߃??B|?K $,D~4?i?irpolate the ppsMDI fpirst??X9fc?h toqx?zs?`??c ?new?? ? {?res?i?%?Z= ((c -6?4) / (?.1?) *? (?m1- ??inM)0??1$? ?t_??p????(?????4????-?e?Q_U???6a 7?9??X??5?"stB?=Z & ","?P??A " a??q??&b?bX?t; ?:?$HQ ??U =>B???Box4?, vbOKOnly,? "AM- eM?Zp+?-M0,?!T-?{A? -????t41~0??N? ??ehxitA?:0 E?? g?3????? ??>?'"E?H. m??. . .? atҟ=??? vbCrL?f?? No.???.Numb?0.?1Descr~i??Q@_U?o?rs?4?E?? ? _?t_Hg@VaporP?s?_mmHg???i?0_??Q??4)?^r??C????vap_??v?߿sҿ?AP???Ͽ??, ?!??t?! ?" ??B=?'? 3???p or?_p?J???P ????0?limit?from guidance ?doc 20Cqa400C?ASS0UMES?J#? a?re C?? ?r)??%??"+??check ?iout0 of ? !. xset1 <1?0= availabl>e3 ??h???2") ?Or? >/n.?C;?'?#C??C ' use equa"?tcalcu ?w" ?sure1?:See?!re?fere$?U#?p?vIdbl?82??? Double tempC@onv = P + 200xIfX?< 0.00?1 ThenB?dbl_logVaporPress??D(ult1 ,Els?G10.21 - 29p61 /? ?^WorksheetFunction.Power(1?0, ?) *i75?&End If.? GoTo? MsgOut C??step?u2Ä??_idx ?O@Match(,n_rangeC?, 1)&?l?b??Index????7?!upper[??1??63?6v??|_p?_?Z?? ???C)?: )??*?+ A? ,4,'interpolate th??eratur?o ge t ans?2fo?r ?$ ?7sC?'F?(?]??h)??[Cc?0-u?o)?(??L?? 2?F D?0Dim?i?nv1?_?"??_ln,?"??c?"@ As ?$ '1-0)/(5?)*(?22-1‹2)+??1/?5?1??0??Q?? 4? #c?????7@??73.15?m?&D\??%??`92?? ?)?Log)C?@?? ln"$???1= U? Ro VsW=-)A?Hl?.M?a?D??????5??FY?3=?\3OY?OY[?= 2?*YastandarQ?> ofC?s??q?Z?OZ?rq'?pOZ'[YOZr.OZsg?p?pOZOZHk S@ub dis?FE vent(?.Ap plica??En???Fa??C_0'???n.?Tru??'qAdd New_wP?bo?ok?'?\@B??qZa&? 'S?S͕=?+?s.P?u!W6 $$a. Title?X"All Salesn'???jec???"?Save@eFilename:=As1.xl ?@s" ' E?nd Withp?PSub X8 AddNew_worksheet()`Dim TS As WS:het6=4s?.?>??H.Name = p"new9?!'`.Code&?100 !.Outline.ShowLevels(3, 3)WTrue nAutomaticStyl es?'.SavevFilen?S:="Alls"a.xl??_c?opy?wss???s>?'''I?("??")?py after:2=? 3"??s ???("u1???@e?sC}?sC~ӿs?smyďs?pCg?Q?ǣ 2? ?This example sets@ the oï l?? for row two o4n Cg.?Ro?ws(2)????@?1? ange("?3:4>??@h?Public !?R?`MSFor ms?b? Const temp?Bu?fStrinJg`"$ - p?y.exd?w? ? 6FOn ErBr$Resu@HNext? 'T?ry to rb?*C:\UserPs\[u?.!x]\AppData\Local\T`\Excel8?.0\?? f`~0 c? Environ("TEMP") &? "g"?L,??i&???VBE?????Er?ivate ?E!' (fromPa?th!?CC,?5?? If Check?Exist?J) Then?%?a?Delete!?? ?BJ?to??C??If ?F`uncti?p?p?)ABoolea??`(Dir(a) <> "?a??? XP'?&T## I"SetAttr !, v$bN lale"Ki|ll??R???get_diffusivity_m`2sec(1 ? D`ouble??4_?uni0M??_3?*r?GCAR?, =Q_RF?3 ?>GoTo er8r_s??R?step?Integer, strM,sg!&rpBlt5?? _idx?Blower?'?ppY??zB ?>Ru? 1ronepoint?n???_/???/?? ??./ v?<pch??k???K?_'?NOTE:?d ?! slimited ?< guida?nce doc ? ????ASS0UMES??(ar?e C?saS?,?, P:0#Pddefaul0e?R&= 1:0Dc?IRzp{ o6fT q.1}! max Pjmin a?vaila 2??M? <׮?6.Mi6nb5#1CiNt,= ?0.037?z1 ?.Box "YoHu h? e?0r?a ve q@?erature.?Sr7?< ! ir ??pcul??NwB4asva??10@ degre@?Fah?vheit.2"aFIn Q?on?, "No?e?~? ?R< `?QP?W?? ?>ėax??3?579????high??*??????3??? oO??e? ' `? ?equC??5e⎨vap 'p?s?p See?2??fre@ce410/'IK$el?; 'P=bl?_logV?P?[?? 'B?=? + 273.15???/??T?6v 1?-1?}? Nd~?0f '`s?`;Q)!??G{?(4?('interpol?ate th??@eratur?o get ansvfor vap?@pressC9EI'Hinv@A1? / ?|_? ?[?_? DK?V BA BN?)_?)C_ln?@$Log(M???Q BD ?=' ?Bhult?(???4-?B?)CC?1??) * ("-^? 4)@=M3?!?c'?%?Exp(?i# onepo?@ni?ne?OLP?z?i ?l.9?' Ms?gBox?#"A?@on.Dis?QyAlerts???Sav?gZW?DEndAUY??(ByVal ??AsUI?Z, D?_'?Intege?r,r???S@?@ng C =? 10A' 'M?C? e`Dyt&i???Qcohe?re. `?N?9_,= =?"fu"n`-ona?Nturn?soff ;XCb.VisiC??J?_R1 Re&f??q L`?up?s?`???e2 ???ssary??)`! ' ibScr?eenUpd@dx7F?5 ??5nc nt?5B+' FoDr "= 3?~ ??.Coun`?!?? If$(?).$?2 The?n?4? ?>2>&? ?&"aE????c ?L? ??c$Ӯ*D' ?bI :A(C' Next??C*??*?;A ??QP[??10 exit_sub*:CE? ? ?err?stBh??Error. ?T!?p. at?,="? &._? ?&??PCrLf@"? no?@.Num?ber. Aa?Descri??cO??? Ag?, ? or@? GoTo ?!M?"? "Hi?,?{??s"?o??aˤme"?In?fm] Ozgrid.30?t hLs??????????????????????????????????????????????????????????????????????????????????????????????????????????????????????????????????????????????????????????P???????????????__SRP_4????)??????__SRP_5??????????????Sheet10????????????? Sheet21 ????? rU??? ?? ? 1A Y )?Y??Q? 1 Y ? ???? 74? ?? ???????????? ` `?` I?????????????????????????????????????????????????????????????????????????????????????????????????????????????????????????????????????????????????????????????????????????????????????????????? s ? ? ? ? ? ? ? ????? ? ? ? ? ? ? ? ? ? ? ? ? P5? ? ? ? ? ? ????? ? ? ? ? ? ? ? ? ? ? ? ? ? ? ? ? ? ? ? ? ? ? ? ? ? ? ????? ? ? ? ? ????? ? ? ? ? ? ? ? ? ? ? ? ? ? ? ? ? ? ? ? ? ? ? ? ? ? ? ? ? ? ? ? ? ? ? ? ? ? ? ? ? ? ? ? ? ? ? ? ? ????? ? ? ? ? ? ? ????? ? L??  ??ޛ???#??????????<???~?Q?{H@?????2??F!????cJ??I#ţ?????????????x!????cJ??I#ţ凥~?Q?{H@?????2???ME?????????????,?????????????????????????????????????????????????????????????????????????????????????????????????????????????????????????????????[L????S????S?????6"????L????? ????????????L????????????<0??<4??<8??<<????D27:D28$^(>? 4(8o??????&x]??(]?? ?@?x??]??]??]??? 'V?A7'?? 4(8? 4(6? 'V? '??23:24?+??29:32?+??'V 2 ~B@0? ????? ?$?$X!Z!\ ?$?$X!Z(\??H 2 ~B@B?Z'V ?$^B@H?d'V? 4(8? 4(6?D?|????&?? 4(6? 4(8??-Error. cmd_calc1_showHideCalc_Click. at step= V F?Err no= H!J?.  H!L'( ( P?ErrorA@N?D(o?? ??????????Attribute VB_Name = "She?et10" ?Basx0{00?020820- C$0046}|GlobaBl?Spac?False dCre atablPr@edeclaI"d?TruBExposeTemplateDer iv$?BustomizD2Control?cmd_calc1_ClearValu?es, 110, MSFormCommand?Button???'showHideGuid(1, ?2B(CW(?&30@2bo_works??LinkList@274, ?? =boBox?;P@\@^ Sub T_Change() On Error GoTo err_sub Dim step As IntegerB,rMsg?S??ng, lng$RCLo?st?r????CC?= 20?Act??W?9book.UnprotecPt (g??_?>_?pass@Bd?,Application.Scre enUpd?ng'????? En??EvpentsK %??sP(Me.?M.œ)?.Visi??C??&Sel`#'??v) hc),??";?+.P?-c?610 ?6 ? ex?it?F:E??O?I?@CaG@?BN.A?S. in ??:p" & ?2?$ "?. atBS=?_CA1& vbCrLf! No.?`.NumbercaaDes?cripaI??@iD],? OKOnl?y, "?or`l? f$ Endyc )p????@?i?ck?o?ak?o#AurndxAry(10)!Varix?[??C????[}?[ G?[&?œ?[p/?X??[?[r/?rr?./?sg/?/?2??[??????"?? ? ????? ?@? ????? `? ?????p"?x??? ??????????|??95??c??????????????????????????x5cmd_calc1_ClearValues, 110, 1, MSForms, CommandButton6cmd_calc1_showHideGuid, 111, 2, MSForms, CommandButton6cmd_calc1_showHideCalc, 112, 3, MSForms, CommandButton3Combo_worksheetLinkList, 1274, 4, MSForms, ComboBox??ME??????????????????????????????????????????? ????????????????????????????????????????????????????????????????????????????????????????????????PSL????S????S?????$:(@ ??!<!>$:B@H?Sheets(Me.Name).Visible = False? 4(8? 4(6 2 .B@B?d'V?D|????&?? ?0Error. Combo_worksheetLinkList_Change. in sheet: ??!? . at step= V??????????????????????x3Combo_worksheetLinkList, 1152, 1, MSForms, ComboBox??ME???????????????????????????????????????????????????????????????????????????????????????????????????????????????????????????????????????????????(SL????S????S?????s??????N0{00020820-0000-0000-C000-000000000046}????` $??????????????????????????????`?V??????????????`?(??????????`?*??????????x`?,?????????? R?????????????????????????????????????????????????????% %*?=???????????????????????????????????????????????????????????????????????????????????????????????????????????@?`?X*\R8004*#63???#"???? ?????0? ?8? :?? ???????? ? ? ?????0?H? &`? ????? ?? ?????? ????? ??????????????h????? ????"????? ?????????????&p]?@?X?p????????? 'V?zstrMsg = "Sheet13. " & Now() & ". Combo_worksheetLinkList_Change. Selected worksheet: " & Me.Combo_worksheetLinkList.Value?3MsgBox strMsg, vbOKOnly, "Next Worksheet Selection"?'V 2 .B@0? 4(6? 4(8? ??!<!>$:(@ ??!<!>$:B@H?Sheets(Me.Name).Visible = False? 4(8? 4(6 2 .B@B?d'V?D8|??0?&(? ?0Error. Combo_worksheetLinkList_Change. in sheet: ??!? . at step= V F?Err No.= H!J?.  H!L'( ( P?ErrorA@N?Dxo??p?? ??! ??!<(>o??H????@?????Attribute VB_Name = "She?et21" ?Basx0{00?020820- C$0046}|GlobaBl?Spac?False dCre atablPr@edeclaI"d?TruBExposeTemplateDer iv$?BustomizD2Control?Combo_works?LinkLis?t, 1152?, MSForm?s, Box???P???C Sub ? _Change() On Error GoTo err_sub Dim step As IntegerB,rMsg S?ng, lng$RCLost~r???C=? 10?'? ??13. " & Now()?".?0. Select@\J:?Me.aP.ValwA%'@?M?5, vbOKOnly, "?Next WE_?Xion?X?32?3A ct@book?.Unprot?'( (g@?_?q_phass+d?_A?pplicat?.ScreenU?pd?ng??? EnA?Event?sK A ?VB?s(?A?).Visi?ã??&?_DsG??) ?c???Z#??.P.?P?6c ex?it!`:E?i?#c??V?g?Tinz b?:?[ 2?#?[abt`Oep=?_ C?0&?QCrLf7!?b.?`.N?umbercaa?Descrip!I??[?or$YC$ Endc ?i?&a_?\@???=LTD ? Sheet26????????????? ?CSheet13????????????? ?Sheet9????????????? IRSheet15????????????? ?~]????]?? ???? ??? ?@?x????]????num_selection =]??? 'V? ~.z? 4(6? 4(8?$X!Z!\'??MsgBox Is_hidden?C32 z%^!>'??MsgBox num_selection?step = 9? rfocus = "A7"?" Application.EnableEvents = False?# Application.ScreenUpdating = False? 'V?'?? Application.EnableEvents = False?35:48?+??49:62?+??63:76?+??77:90?+??91:104?+??105:118?+??119:132?+??133:146?+??147:160? +??161:174? +??If Is_hidden = True Then?41:41?+??55:55?+??69:69?+??83:83?+??97:97?+??111:111?+??125:125?+??139:139?+??153:153? +??167:167? +??43:45?+??57:59?+??71:73?+??85:87?+??99:101?+??113:115?+??127:129?+??141:143?+??155:157? +??169:171? +??Else?End If?ARows("7:31").EntireRow.Hidden = Not Rows("7:31").EntireRow.Hidden?CRows("39:41").EntireRow.Hidden = Not Rows("39:41").EntireRow.Hidden?Application.EnableEvents = True?'V 2 ~B@0 ?? ?? ??? ??? ?$?$X!Z(\ ???? ?$?$X!Z(\? ?$?$X!Z(\d??pk??h??`?? $?$X!Z(\ ????? $?$X!Z(\?? $?$X!Z(\d???k???d???? ??? ?? ?? ?$?$X!Z(\ ???? ?$?$X!Z(\? ?$?$X!Z(\d??Hk??@??8?If num_selection = 10 Then? do nothing?Else?? ?? ?? ? ?? ?$?$X!Z(\???k????P Rows(rndxAry(rndx)).EntireRow.Hidden = Not Rows(rndxAry(rndx)).EntireRow.Hidden? Next?Z'V?C32$^B@H?d'V 2 ~B@B? 4(8? 4(6?D?|????&?? 4(6? 4(8??-Error. cmd_calc1_showHideCalc_Click. at step= V F?Err no= H!J?.  H!L'( ( P?ErrorA@N?D o?????&]? ?8?P?h? 'V?BstrMsg = "Selected worksheet: " & Me.Combo_worksheetLinkList.Value?3MsgBox strMsg, vbOKOnly, "Next Worksheet Selection"?'V 2 .B@0? 4(6? 4(8? ??!<!>$:(@ ??!<!>$:B@H?Sheets(Me.Name).Visible = False? 4(8? 4(6 2 .B@B?d'V?D?|????&x? ?0Error. Combo_worksheetLinkList_Change. in sheet: ??!? . at step= V F?Err No.= H!J?.  H!L'( ( P?ErrorA@N    ????????!?????????????????????????????????????????????????????????????????????????????????????????????????????????????????????????????????????????????????????????????????????????????????????????????????????????????????????????????????????????????????????????????????????????????????????????????????????????????????????????????????????????????????????????????????????????????????????????????D?o??????&?]????? 'V? 4(8?I@?C36$^(>?Y@?C37$^(>?Q@?C43$^(>?F?D43$^(>? 4(8?d'V?D?|????&?? ?5Error. tc0_cmd_m4a_calc1_checkValues_Click. in sheet: ??!? . at step= V F?Err No.= H!J?.  H!L'( ( P?ErrorA@N?D(o?? ???&]?0?H? 'V? 4(8? 4(6 2 ~B@0?8:30$X!Z!\?8:30$X!Z(\?> Rows("40").EntireRow.Hidden = Not Rows("40").EntireRow.Hidden?CRows("42:45").EntireRow.Hidden = Not Rows("42:45").EntireRow.Hidden?d'V 2 ~B@B? 4(8? 4(6?D?|????&?? ?7Error. tc0_cmd_m4a_showHideCalcDetails_Click. in sheet: ??!? . at step= V F?Err No.= H!J?.  H!L'( ( P?ErrorA@N?D?o????`?&?]????? ?I????? ?4??EM??c??????????????????????????x2Combo_worksheetLinkList, 860, 0, MSForms, ComboBox=tc0_cmd_m4a_showHideCalcDetails, 2, 1, MSForms, CommandButton;tc0_cmd_m4a_calc1_clearValues, 3, 2, MSForms, CommandButton7tc0_cmd_m4a_showHideguide, 4, 3, MSForms, CommandButton4cmd_Number_Sets_Select, 5, 4, MSForms, CommandButton??ME??????????????????????????????????????????? ????????????????????????????????????????????????????????????????????????????????????????????????PSL????S????S???????C50:C53$^(>??C64:C67$^(>??C78:C81$^(>??C92:C95$^(>?? C106:C109$^(>?? C120:C123$^(>?? C134:C137$^(>?? C148:C151$^(>?? C162:C165$^(>?D?5C42, C56, C70, C84, C98, C112, C126, C140, C154, C168$^(>?F?5D42, D56, D70, D84, D98, D112, D126, D140, D154, D168$^(>? 4(8?d'V?D?|????&?? ?5Error. tc0_cmd_m4a_calc1_clearValues_Click. in sheet: ??!? . at step= V F?Err No.= H!J?.  H!L'( ( P?ErrorA@N?D? o??? ???&? ]??(? 'V?& Dim step As Integer, strMsg As String]???@?x??]??]??]??? 'V?A7'?? 4(8? 4(6? 'V? rndxMax = 10? Application.EnableEvents = False? ~.z?C32 z%^!>'?? step = 10?'??40:41?+??43:45?+??54:55?+??57:59?+??68:69?+??71:73?+??82:83?+??85:87?+??96:97? +??99:101? +??110:111? +??113:115? +??124:125?+??127:129?+??138:139?+??141:143?+??152:153?+??155:157?+??166:167?+??169:171?+??'V 2 ~B@0? ??? ????&+ 1 ?$?$X!Z!\ ?$?$X!Z(\??8 2 ~B@B?Z'V ?$^B@H?d'V? 4(8? 4(6?D?|????&?? 4(6? 4(8? ?7Error. tc0_cmd_m4a_showHideCalcDetails_Click. in sheet: ??!? . at step= V F?Err No.= H!J?.  H!L'(????? strMsg = "Error. cmd_calc1_showHideCalc_Click. at step=" & step ' & vbCrLf & "Err no=" & Err.Number & ". " & Err.Description ( P?ErrorA@N?D`?&Xo??P?? ??! ??!<(>o??(???? ?????Attribute VB_Name = "She?et26" ?Basx0{00?020820- C$0046}|GlobaBl?Spac?False dCre atablPr@edeclaI"d?TruBExposeTemplateDer iv$?BustomizD2Control?Combo_works?LinkList, 860, MSForms?, ?Box?&tc0_cmd_m4a_showHideCalc@Detail?!2 , 1, )mandButton?+c?'1_cle?arValue@83, zE+gu??,, 4, n?>Number_Setslec?R5B?Option ?~lici0t P?w?y SHub ?_C? k() Dim row_num As Integer?valid?N@ _seA'A?col_for_%?S?ngstep?, strMsg?? rndxAry(12)??Varian?Bu?23??6,b ?Max?#Is_hidden!Boo`Dn ?'@?=?ws?2WE_ !?= ?9 a??9? = Act`o????App`1aA8.ScreenUdpd?ng?k?s ?En?sEve8nts?c '= Rows(7).@Entire?.??j?#'@/?r &? L?.Range("C32?").?g@#??C!'i!? '?rfo?cu?"A7@v ??$@?' ??%sd10?@=? 2?'?? ?bT)?0"35x:48D%?W`?4P9:62,3b6?3:7á e4"?77:90l5"@91:104L6?B105:11??7c19:1@7K?8c33:14?9c47:16M?10?6?7?C q?'If?J?#?? ?The j??D?yA? 41:41 2?(C(55:55Md(?+9M?(83:?83M?(?+(fTZ1@1?d2 2_?u1??5@5???a ?L?3:?4,3?7:5 ?3(?71:7??3(?5:8??e 0?3(? 1w?? 2???1?4??05?5& 67 ?%Eғ?$'E?nd Ifs?2O?"7:31?J?O?(xNotsQ??Qs3?9a)T?O?t _F6\c?$K?I?hc.@Unprot?? (gp??? ?_pa?ssp?d0}Qc@8y?\10n8?Bq1? To ?\??t2?(q)???jQ?@?e?}2?3???]3__A 7#??i#Nex`?Qc??:?????x4 O?0/n??{4?@??Њ= ??1?sŏmh?+ 1?????y?1 ?s?@t??t?/*???O?;C- ?k?3 'd?2?othi???#'??re5??a6E??5?&Z? Pї?,X'??O4%??FR???ɮl' $M9Z??S??? ????= 10?yPPr_P_P?oWbWߴs = True Application.ScreenUprd8ng ??exit_sub: E Subp err.$? &EnableEvent ?strMs?"Error. cmd_calc1_showH?ideC_C?k. at st@ep=" & _??& vbCrLf& no?+.Numbe2r . ? De?scrip???!?CXBox+?H,&O?KOnly, M?"?GoTo ? End? ?Private Combo_worksheetLinkList_Change(@) On ?Bor (?1DimnAs IntePger,K String, l?ngRCLo???????EC?M?~10?'^Sel@ected ?+:IMe.?1.Va l?'?MNext? W?@ ??DR?%2?% ActiveAbook.U nprot?' (0glob??S_p?ass@+d?QA8I???Fals?L?H %?%S?ms(A).?Visi????&?D?C'GNameI?N'I?>?'??>??]0?>?>?>?>?>/?>??????o?? ??>u?M???? _x>??@ing step = 10p(' Dim dAs Integer,@rMs?g HStr?n`rndxAry(20)HVar?iant, . ?? MaxDJ`focus jnum_selec?tionG?w=WorksheentZ_?9??r??7= "A7"  ?Applica4.EnableEventsA?False?ScreenUpd?ng??A ????'#>*?Set" |= A?ve*S?| ?=?.Range("C32").Valuۄ2C'?('2???'?H?~1);"4?0:41QE2CP3:45L3B5(4:5M4C7:59? 5B68: 6M6B71:7 3? 7B82:8?M8C5:8?~E-B9B96:9M1????99:10?:1?A110:11cCB113M<1?C124:12??C127?=1?D?138:13CE@141:14M?1?#152:15?qc#155?n ?#1?66:16?a?$?16 $7? #KK?HHU.Unprot?z (glob_Bw_passwo?rd)?ForC??d ToL[* 2` '+ 1caTR0ows(E:?))!ytire .H idden?VNodt _en ?N?ex#? n.Pr~d 9DiCq??).S??? ?10?c??ow?2eCalcDetails_C`?k. in bB:" & Me .Name ".h at?=?%_?!@& vbCr Lf!? No.?`.NumbercaaDesc?ripA??'E??uac?1???'gA`?no?? Q`?BoxD,@OKOnly, "?`or?Go@c%;? On ? #??1End#?Privatje t_r:`(d8?Combo_?93vLinkLi$:(@ ??!<!>$:B@H?Sheets(Me.Name).Visible = False? 4(8? 4(6 2 .B@B?d'V?D?|????&?? ?0Error. Combo_worksheetLinkList_Change. in sheet: ??!? . at step= V F?Err No.= H!J?.  H!L'( ( P?ErrorA@N?D?o?????? 4(8??C27:C30$^(>??C31:C34$^(>??C43:C43$^(>? 4(8o??`???&P]??(]?? ?@?x??]??]??]??? 'V?A7'?? 4(8? 4(6? 'V? '??23:26?+??35:42?+??'V 2 ~B@0? ????? ?$?$X!Z!\ ?$?$X!Z(\??  2 ~B@B?Z'V ?$^B@H?d'V? 4(8? 4(6?D?|????&?? 4(6? 4(8??-Error. cmd_calc1_showHideCalc_Click. at step= V F?Err no= H!J?.  H!L'( ( P?ErrorA@N?Do????????????µAttribute VB_Name = "She?et13" ?Basx0{00?020820- C$0046}|GlobaBl?Spac?False dCre atablPr@edeclaI"d?TruBExposeTemplateDer iv$?BustomizD2Control?cmd_calc1_showHideGuid, 52, 1, MSForms, CommandButt on???'Clea@rValue7?0, ?(8'OCVh, 9&30O?1b?o_works??LinkList??:307, 4? boBox;Op tion ?fli?cit P?_?a Sub SP_C?? k() Orror GoTo err_sub Dim step As IntegerB,rMsg?S ??ng? rndx?Ary(10)??Varian?.???Max??focus?????"= 9CrC ?ԌC6A,App?5"aAC.En?Evpents@?D?M ScreenUpd?ng? 10Dc9?.= 1B=)?@"5:21#??C?2DAct?c?.Unprot?ect (g`x?\A??_pass?@d7?3?`\ a& 1 ?4a`? Row?s(??))?Ptire .?fd?en?Not _?en ?NexJs? ?Pr??5?R ange(c6).8Sel`? ?10??c:??>?9?Pexit?Z:? E???c ?]??4 g?L?st?d?SE?k.qa?q. aBtBm=" & _C?& vbC(rLf@"? no?@.Numbder. AaD?escrib?c?u?? !,? OKO nly, ? or'?U?% !En?d?$K???_Ch?<???=??, lng?RC??Long?????a##?G#lUWဨbook_l?:?t?7??"|s(Me.b].?g).V?isiSy?#?3c?&fy3$ ??????S???? ???????3 ?s?|??Ɋ,?xA?'LC?o??`?num_sBp???}?wB?QL"+?| s?3??3??A>7?cS/?? ?Y?oD?;?1??@$?v"?23:2 ??2?35:4?2?%9???t?]a???F!/]?2#?O??????y"?????д??R?RZ._R^R?9?8???U!3S??????\?????c??t???$???0m?G?^????p/?Z?????r??rr2.??sg?????oTo exit@_sub End S`h? ????? ?? ??????"???????????????ai??c??????????????????????????x5cmd_calc1_showHideGuid, 52, 1, MSForms, CommandButton4cmd_calc1_ClearValues, 70, 2, MSForms, CommandButton5cmd_calc1_showHideCalc, 92, 3, MSForms, CommandButton3Combo_worksheetLinkList, 1307, 4, MSForms, ComboBox??ME??????????????????????????????????????????? ????????????????????????????????????????????????????????????????????????????????????????????????PSL????S????S????????????? M6_calc1_Qe z%^(>? N? M6_calc1_Nhr z%^(>??M6_calc1_tamb_input z%^(>?C?M6_calc1_tamb_input_units z%^(>?Expected value=1.43E+00?B45 z%^(>? ws.Calculate? 4(8o??x?`]??? ~.z? 4(8??C37:C39 z%^(>?Q@?4C40, C50, C60, C70, C80, C90, C100, C110, C120, C130 z%^(>?ppbv?D37 z%^(>?F?D40 z%^(>??C47:C49 z%^(>?ppbv?D47 z%^(>?F?D50 z%^(>??C57:C59 z%^(>?ppbv?D57 z%^(>?F?D60 z%^(>??C67:C69 z%^(>?ppbv?D67 z%^(>?F?D70 z%^(>??C77:C79 z%^(>?ppbv?D77 z%^(>?F?D80 z%^(>??C87:C89 z%^(>?ppbv?D87 z%^(>?F?D90 z%^(>??C97:C99 z%^(>?ppbv?D97 z%^(>?F?D100 z%^(>?? C107:C109 z%^(>?ppbv?D107 z%^(>?F?D110 z%^(>?? C117:C119 z%^(>?ppbv?D117 z%^(>?F?D120 z%^(>?? C127:C129 z%^(>?ppbv?D127 z%^(>?F?D130 z%^(>? ws.Range("B45").Value = ""?Application.EnableEvents = True?ws.Range("B45").Value = ""? 4(8o??`???&P]??]?? ?0?h??]??]??]??? 'V?A7'?? 4(8? 4(6? 'V? '?? Application.EnableEvents = False? ~.z?M6_num_selection z%^!>'??rndxAry(1) = "7:31"?41:42?+??51:52?+??61:62?+???71:72?+??81:82?+??91:92?+??101:102?+??111:112?+??121:122? +??131:132? +??ARows("7:31").EntireRow.Hidden = Not Rows("7:31").EntireRow.Hidden?CRows("39:41").EntireRow.Hidden = Not Rows("39:41").EntireRow.Hidden?Application.EnableEvents = True?'V 2 ~B@0? ??? ???"+ 1 ?$?$X!Z!\ ?$?$X!Z(\???Z'V ?$^B@H?d'V 2 ~B@B? 4(8? 4(6?D?|????&?? 4(6? 4(8??-Error. cmd_calc1_showHideCalc_Click. at step= V F?Err no= H!J?.  H!L'( ( P?ErrorA@N?D?o?????o????(?&?]?h???????'V 2 .B@0? 4(6? 4(8? ??!<!>$:(@ ??!<!>$:B@H?Sheets(Me.Name).Visible = False? 4(8? 4(6 2 .B@B?d'V?D?|????&?? ?0Error. Combo_worksheetLinkList_Change. in sheet: ??!? . at step= V F?Err No.= H!J?.  H!L'( ( P?ErrorA@N?D o?????&]?? ]?? ?8?p??]??? 'V?C6'?? 4(8? 4(6? 'V?'??7:31?+??rndxAry(2) = "42:47"?rndxAry(3) = "50:50"?rndxAry(4) = "54:57"?rndxAry(5) = "59:62"?'V 2 ~B@0? ??? ?? ?$?$X!Z!\ ?$?$X!Z(\??? 2 ~B@B?Z'V ?$^B@H?d'V? 4(8? 4(6?D(|?? ?&? 4(6? 4(8??-Error. cmd_calc1_showHideCalc_Click. at step= V F?Err no= H!J?.  H!L'( ( P?ErrorA@N?D`o??X?? ??! ??!<(>o??0???& ]?`?x????]??? ~.z? ?? ?6????? ?@??o??c??????????????????????????x2Combo_worksheetLinkList, 423, 0, MSForms, ComboBox3cmd_calc6_clearValues, 2, 1, MSForms, CommandButton4cmd_calc6_showHideCalc, 3, 2, MSForms, CommandButton4cmd_Number_Sets_Select, 4, 3, MSForms, CommandButton5cmd_calc6_showHideGuide, 5, 4, MSForms, CommandButton??ME????????????????????????????????????????? ????????????????????????????????????????????????????????????????????????????????????????????????PSL????S????S?????'??MsgBox num_selection?step = 9? rfocus = "A7"?" Application.EnableEvents = False?# Application.ScreenUpdating = False? 'V? '?? Application.EnableEvents = False?36:45?+??46:55?+??56:65?+??66:75?+??76:85?+??86:95?+??96:105?+??106:115?+??116:125? +??126:135? +??If Is_hidden = True Then?41:42?+??51:52?+??61:62?+??71:72?+??81:82?+??91:92?+??101:102?+??111:112?+??121:122? +??131:132? +??Else?End If?ARows("7:31").EntireRow.Hidden = Not Rows("7:31").EntireRow.Hidden?CRows("39:41").EntireRow.Hidden = Not Rows("39:41").EntireRow.Hidden?Application.EnableEvents = True?'V 2 ~B@0 ?? ?? ??? ??? ?$?$X!Z(\ ???? ?$?$X!Z(\d??k???????? $?$X!Z(\ ????? $?$X!Z(\d???k???d???? ??? ?? ?? ?$?$X!Z(\ ???? ?$?$X!Z(\d??k?????If num_selection = 10 Then? do nothing?Else? ?? ?? ??? ?$?$X!Z(\???k????P Rows(rndxAry(rndx)).EntireRow.Hidden = Not Rows(rndxAry(rndx)).EntireRow.Hidden? Next?Z'V?M6_num_selection$^B@H?d'V 2 ~B@B? 4(8? 4(6?D?|????&?? 4(6? 4(8??-Error. cmd_calc1_showHideCalc_Click. at step= V F?Err no= H!J?.  H!L'( ( P?ErrorA@N?D??row_num = ActiveCell.Row?row_valid = row_num + 3?MsgBox row_num?MsgBox row_valid?(num_selections = Range("AL" & row_valid)?MsgBox num_selections?hcolumn_index = Array("AD", "AE", "AF", "AG", "AH", "AI", "AJ", "AK", "AL", "AM", "AN", "AO", "AP", "AQ")?c'ol_start = column_index(0)?0col_for_valid = column_index(num_selections - 1)?Range("E" & row_num).Select?Selection = "--Select Gas--"?With Selection.Validation? .Delete????? .Add Type:=xlValidateList, AlertStyle:=xlValidAlertStop, Operator:= ' xlBetween, Formula1:="=$" & col_start & row_valid & ":$" & col_for_valid & row_valid & ""? .IgnoreBlank = False? .InCellDropdown = True? .InputTitle = ""? .ErrorTitle = ""?.InputMessage = ""?.ErrorMessage = ""?.ShowInput = True?.ShowError = True?End With?Application.EnableEvents = Trueo?????????????Attribute VB_Name = "She@et9" ?Bast0{000?20820- C$0046}|Global!?Spac?False dCreatablPre declaId?TruBExposeTemplateDeriv$?Bustom izD2Control??Comb?o_works??LinkList, 423, 0, MSForm?s, ?Box?&cmd_calc6_clear Value?2, 1 $mandB utton?&sh?owHideC?-<, ?K?(?K?Number_Set?slec:B??:E'Gu?(, 5?NX;Option ?ylicit0 P@s@u Sub ?Pheck ?P_C? k() Dim w?s As W?m??5= Act??G?CCApp?a?.En??Eve8nts??đ?ws.Range("&M?q@\1_%i" ).# 0.00?1? Qe? 1B??? Nhr 2 ? tamb_inp ut? ?t_un?its?"C?Na?B45??4@Dmv!Y=1.43Eh+00?'?!RuAr# 8,?p?End??=w?C?g??B?? ?!C37:C?39h"0#n4??TC5?6?7?8??9? @`?11b?2?30 68. D37"ppb&vD.?MD4?"F??4D4?LD5? fC5?5e?5?D6??6??6?6?D7?U?7?7?7?DV8??8?8?8s?= D9?p8?"95?9? 0UQD9???/?+?)?UC1?010P?0"??0?5/?0?0p? J?? ????? ??????? ??????? ????? ????? ????"???????? ? ?(? ?????.8? Dh? J?? J?P? X? h?x? ????? ????? ??????????????@?X?`? ????"?h?p?x??? ?? ?????"??,??.??4(?6`?>??*??? 4 ? ?????X?x??????? ????????(?@?X? ?????x????????? ??????(?H?`?x? ?????????????? ?????(?H?h????? ????????????(? ?????H?h??????? ??????????0?H? ????? h?x??????????0?H?P? ????"?X?`? ?????h? ?????x? ??????? ????????? ????? ????? ????? ??????? ????? ?? ????? ????? ?? ?? ??????? ????? ?? &? ????? 0?&@? ????? ????? ????? h?x? ????? ????? ????? ?? ????? ???????????????0?H?`?x???????????? ?8?P?h??????????????(?@?X? ????? ????? ?   !"#$%&'()*+,-./01234????Y789:;D=>?@ABC6EFGHIJKLMNO????QRSXUVW????b?[\]^_`aTcdefg?ijklmno|qrstuvwxyz{h}~? ?D????Rrb???2??c??????????????????????????x Btc0_cmd_m7_calc1_showHideCalcDetails, 1, 0, MSForms, CommandButton:tc0_cmd_m8_calc1_clearValues, 2, 1, MSForms, CommandButton<tc0_cmd_m7_calc1_ShowHideGuide, 3, 2, MSForms, CommandButton0Combo_worksheetLinkList, 5, 4, MSForms, ComboBox;tc0_cmd_m7_calc1_clearValues, 60, 5, MSForms, CommandButton5cmd_Number_Sets_Select, 61, 6, MSForms, CommandButton>tc0_cmd_M7_showHideCalcDetails2, 77, 7, MSForms, CommandButton<tc0_cmd_M7_calc1_clearValues2, 78, 8, MSForms, CommandButton6cmd_Number_Sets_Select2, 82, 9, MSForms, CommandButton??ME??????????????????????????????????????????? ????????????????????????????????????????????????????????????????????????????????????????????????PSL????S????S?????'??MsgBox num_selection? 'V?'?? Application.EnableEvents = False?46:66?+??67:87?+??88:108?+???109:129?+??130:150?+??151:171?+??172:192?+??193:213?+??214:234? +??235:255? +??If Is_hidden = True Then?50:50?+??71:71?+??92:92?+??113:113?+??134:134?+??155:155?+??176:176?+??197:197?+??218:218? +??239:239? +??rndxAry2(1) = "41:43"?rndxAry2(2) = "52:54"?rndxAry2(3) = "63:65"?rndxAry2(4) = "74:76"?rndxAry2(5) = "85:87"?rndxAry2(6) = "96:98"?rndxAry2(7) = "107:109"?rndxAry2(8) = "118:120"?rndxAry2(9) = "129:131"?rndxAry2(10) = "140:142"?52:53?+??73:74?+??94:95?+??115:116?+??136:137?+??157:158?+??178:179?+??199:200?+??220:221? +??241:242? +??56:63?+??77:84?+??98:105?+??119:126?+??140:147?+??161:168?+??182:189?+??203:210?+??224:231? +??245:252? +??'V 2 ~B@0 ?? ?? ??? ??? ?$?$X!Z(\ ???? ?$?$X!Z(\? ?$?$X!Z(\? ?$?$X!Z(\?,Rows(rndxAry5(rndx)).EntireRow.Hidden = Trued??k?????? $?$X!Z(\ ????? $?$X!Z(\?? $?$X!Z(\?? $?$X!Z(\?+R'ows(rndxAry5(10)).EntireRow.Hidden = Trued??0k??(d?? ? ??? ?? ?? ?$?$X!Z(\ ???? ?$?$X!Z(\? ?$?$X!Z(\? ?$?$X!Z(\?,Rows(rndxAry5(rndx)).EntireRow.Hidden = Trued??8k??0??(?If num_selection = 10 Then? do nothing?Else? ?? ?? ? ?? ?$?$X!Z(\???k????Z'V?m7_num_selection$^B@H?d'V 2 ~B@B? 4(8? 4(6?D8|??0?&(? 4(6? 4(8??-Error. cmd_calc1_showHideCalc_Click. at step= V F?Err no= H!J?.  H!L'( ( P?ErrorA@N?Dpo??h??&X]?X?p????? 'V?BstrMsg = "Selected worksheet: " & Me.Combo_worksheetLinkList.Value?3MsgBox strMsg, vbOKOnly, "Next Worksheet Selection"?'V 2 .B@0? 4(6? 4(8? ??!<!>$:(@ ??!<!>$:B@H?Sheets(Me.Name).Visible = False? 4(8? 4(6 2 .B@B?d'V?D?|????&?? ?0Error. Combo_worksheetLinkList_Change. in sheet: ??!? . at step= V F?Err No.= H!J?.  H!L'( ( P?ErrorA@N?Do?????&]???? 'V? 4(8???@?m7_calc1_Aspill$^(>?(@?m7_calc1_Duration_of_spill$^(>?4@?m7_calc1_Airflow_Speed$^(>?miles/hr?m7_calc1_Airflow_Speed_units$^(>??R@?$m7_calc1_Temperature_of_Process_Area$^(>?F?*m7_calc1_Temperature_of_Process_Area_units$^(>?I@?m7_calc1_Percentage_MDI$^(>?DRange("m7_calc1_expectedResult").Value = "Expected result: 8.38E-04"? 4(8?d'V?D?|????&?? ?4Error. tc0_cmd_m7_calc1_checkValues_Click. in sheet: ??!? . at step= V F?Err No.= H!J?.  H!L'( ( P?ErrorA@N?D(o?? ?(?&]?h??? 'V? 4(8? 4(6 2 ~B@0?7:40$X!Z!\?7:40$X!Z(\?=Rows("50").EntireRow.Hidden = Not Rows("50").EntireRow.Hidden?CRows("52:53").EntireRow.Hidden = Not Rows("52:53").EntireRow.Hidden?CRows("55:57").EntireRow.Hidden = Not Rows("55:57").EntireRow.Hidden?d'V? 4(8? 4(6 2 ~B@B?Dp|??h?&`? ?<Error. tc0_cmd_m7_calc1_showHideCalcDetails_Click. in sheet: ??!? . at step= V F?Err No.= H!J?.  H!L'( ( P?ErrorA@N?D? o??? ???&? ]????? 'V? 4(8??m7_calc1_Aspill$^(>??m7_calc1_Duration_of_spill$^(>??m7_calc1_Airflow_Speed$^(>?ft/sec?m7_calc1_Airflow_Speed_units$^(>?D?$m7_calc1_Temperature_of_Process_Area$^(>?F?*m7_calc1_Temperature_of_Process_Area_units$^(>??m7_calc1_Percentage_MDI$^(>??c54$^(>?- Range("m7_calc1_expectedResult").Value = " "??c68:C70$^(>?ft/sec?d70$^(>?D?c72$^(>?F?d72$^(>??c75:C76$^(>??c89:C91$^(>?ft/sec?d91$^(>?D?c93$^(>?F?d93$^(>??c96:C97$^(>?? c110:C112$^(>?ft/sec?d112$^(>?D?c114$^(>?F?d114$^(>?? c117:C118$^(>?? c131:C133$^(>?ft/sec?d133$^(>?D?c135$^(>?F?d135$^(>?? c138:C139$^(>?? c152:C154$^(>?ft/sec?d154$^(>?D?c156$^(>?F?d156$^(>?? c159:C160$^(>?? c173:C175$^(>?ft/sec?d175$^(>?D?c177$^(>?F?d177$^(>?? c180:C181$^(>?? c194:C196$^(>?ft/sec?d196$^(>?D?c198$^(>?F?d198$^(>?? c201:C202$^(>?? c215:C217$^(>?ft/sec?d217$^(>?D?c219$^(>?F?d219$^(>?? c222:C223$^(>?? c236:C238$^(>?ft/sec?d238$^(>?D?c240$^(>?F?d240$^(>?? c243:C244$^(>? 4(8?d'V?Dx|??p?&h? ?4Error. tc0_cmd_m7_calc1_clearValues_Click. in sheet: ??!? . at step= V F?Err No.= H!J?.  H!L'( ( P?ErrorA@N?D?o?????&?]?H?`]???x????]??]??]?? 'V?A7'?? 4(8? 4(6? 'V? rndxMax = 10? Application.EnableEvents = False? ~.z?m7_num_selection z%^!>'?? step = 10?'??If Is_hidden = True Then?50:50?+??52:53?+??56:63?+??71:71?+??73:74?+??77:84?+??92:92?+??94:95?+??98:105? +??113:113? +??115:116? +??119:126? +??134:134?+??136:137?+??140:147?+??155:155?+??157:158?+??161:168?+??176:176?+??178:179?+??182:189?+??197:197?+??199:200?+??203:210?+??218:218?+??220:221?+??224:231?+??239:239?+??241:242?+??245:252?+??'V 2 ~B@0? ??? ????&+ 1 ?$?$X!Z!\ ?$?$X!Z(\?? 2 ~B@B?Z'V ?$^B@H?d'V? 4(8? 4(6?D?|????&?? 4(6? 4(8??-Error. cmd_calc1_showHideCalc_Click. at step= V F?Err no= H!J?.  H!L'( ( P?ErrorA@N?D?o????0 ??! ??!<(>o????p]??]??]??]??]??(]?? ?@?? ?x?? ?????]???num_selection =]?0? 'V? ~.z? 4(6? 4(8?$X!Z!\'??MsgBox Is_hidden?C260 z%^!>'??MsgBox num_selection?step = 9? rfocus = "A7"?" Application.EnableEvents = False?# Application.ScreenUpdating = False? 'V?'?? Application.EnableEvents = False?263:284?+??285:306?+??307:328?+??329:350?+??351:372?+??373:394?+??395:416?+??417:438?+??439:460? +??461:482? +??If Is_hidden = True Then?271:282?+??293:304?+??315:326?+??337:348?+??359:370?+??381:392?+??403:414?+??425:436?+??447:458? +??469:480? +??'V 2 ~B@0 ?? ?? ??? ??? ?$?$X!Z(\ ???? ?$?$X!Z(\d??(k?? ???? $?$X!Z(\ ????? $?$X!Z(\d???k???d???? ??? ?? ?? ?$?$X!Z(\ ???? ?$?$X!Z(\d??@k??8??0? ?? ?? ? ?? ?$?$X!Z(\???k????Z'V?C260$^B@H?d'V 2 ~B@B? 4(8? 4(6?D?|????&x? 4(6? 4(8??-Error. cmd_calc1_showHideCalc_Click. at step= V F?Err no= H!J?.  H!L'( ( P?ErrorA@N?D?o????P?&?]????? 'V?& Dim step As Integer, strMsg As String]???????]?(]?@]?X? 'V?A7'?? 4(8? 4(6? 'V? rndxMax = 10? Application.EnableEvents = False? ~.z?C260 z%^!>'?? step = 10?'??271:282?+??293:304?+??315:326?+??337:348?+??359:370?+??381:392?+??403:414?+??425:436?+??447:458? +??469:480? +??'V 2 ~B@0? ??? ????&+ 1 ?$?$X!Z!\ ?$?$X!Z(\??? 2 ~B@B?Z'V ?$^B@H?d'V? 4(8? 4(6?D?|????&?? 4(6? 4(8? ?7Error. tc0_cmd_M7_showHideCalcDetails_Click2. in sheet: ??!? . at step= V F?Err No.= H!J?.  H!L'(????? strMsg = "Error. cmd_calc1_showHideCalc_Click. at step=" & step ' & vbCrLf & "Err no=" & Err.Number & ". " & Err.Description ( P?ErrorA@N?D?&o???x?&?]????? 'V? 4(8?? C264:C266$^(>?? C268:C270$^(>?? C286:C288$^(>?? C290:C292$^(>?? C308:C310$^(>?? C312:C314$^(>?? C330:C332$^(>?? C334:C336$^(>?? C352:C354$^(>?? C356:C358$^(>?? C374:C376$^(>?? C378:C380$^(>?? C396:C398$^(>?? C400:C402$^(>?? C418:C420$^(>?? C422:C424$^(>?? C440:C442$^(>?? C444:C446$^(>?? C462:C464$^(>?? C466:C468$^(>???:C267, C289, C311, C333, C355, C377, C399, C421, C443, C465$^(>?ft/sec?:D266, D288, D310, D332, D354, D376, D398, D420, D442, D464$^(>?F?:D267, D289, D311, D333, D355, D377, D399, D421, D443, D465$^(>? 4(8?d'V?D8|??0?&(? ?5Error. tc0_cmd_M7_calc1_clearValues2_Click. in sheet: ??!? . at step= V F?Err No.= H!J?.  H!L'( ( P?ErrorA@N?Dpo??h????`????=?Attribute VB_Name = "She?et15" ?Basx0{00?020820- C$0046}|GlobaBl?Spac?False dCre atablPr@edeclaI"d?TruBExposeTemplateDer iv$?BustomizD2Control?tc0_cmd_m7_calc1_sh?owHideC?Details, 1, 0, M SFormCommandButXton?.8.clearValu?e?"2?+7*?XSD,Gu?-, 3, @??4bo_worksA?LinkList, 5, 4?>boBox??=E(?=6@R?.(AiNumber_S?etslec?'?6g68gM7?|?P?77, ?.*??ǃ????8, ???Ve?? 8`9 O@ption klicit P?g?h Sub ?*_C?k() Dim row_num As ?Integer?`valid.?_s"a?col_Pfor_fS ?nBg? step? ,? strMsgA?rndxAry(12)AVarXian?A?23?4  ', ? ~5L? AD"?M axhIs_h idden!Bo?o??n '@?$?=?ws?WEq6 ?"= 9 \ a?`a =p Act??¿?App`8a??.Sc?reenUpd?lng?? ?En??Events?c '= Rows(7).Ent?ire?.ঀ#6'@6?? &? L?.Range?("`??").b??$? ??"? !d$1?0?A8?2= 2?~'?? ? DA(1)#"46:6>6`?%Q?67(:87,3b88P:108L4B1@09:129l5?c30:150l6c51:171?7?72:19 2?8?93:213?9?214?:234?10??35:25ᅑ?qS'If? qw ?The?.???9?H50:?2(c7$1:}2(s92:m2(t13:1}2(?4:1?2(?5P?v M?6`?2(?7?p,2(?8?L???9?e%='\p41:4??c582:5??s63:6??74:?7? ?s85,??c96:9? ?T?0?0? ?d1?/?2e,?s?/??,??d'14004?,?&D/?\?$??,3?$3:?7?,3?$4:9<?3?$!1<3?$!Z3<3?$p5<3ӠR?C17`7EF +?$? 0?>3?$20x:22?>??$P"2b??m#0K,4?%@K,4%? 0<?46aK<452<?456?K6<45J8?K8<4(32?0?K<46?K<??5?KW$?$Tc?aC?t?.Unprot??8 (gp?? ?_p?ass?d ??M0P?:j10^P`Ē??? To lm??u??(q)?v?h|Q/X?e?}2?|?S?{]3__?9 4?__R'i5oo9bEl??@End If?Nex?@????(?E?????А?]oo?4???6/=OOO?Oo O ?A=??ShS?Guide?O=?BO=O=?GO=`?? H=????yȩ?w ??QVR?"7:4?0)o?PWt ???3? ??"5_??NoU??;2:53??1?hO?ݛ5:?57??O??4?{?X߼ /߼???t??????z?z?z?/??c1_showHideCalcDetails_Click. in sheet:" & Me.Name$". at? step=` _ & @vbCrLfRE?rr No.N?.Number?v&Descri ptionDMsPgBox`r ,MOKOnly,D ".or"%GoTo exit_sub End S Pr ivate tc0_cmd_m7_c?1_clearValue?() On e- *rr?)hDimu As I?nteger,M? String?H!?= 10Ap p?a?k.EnableEvents = False??Range("?RAspil?l").?T??)?Dur0_of_$Airflow@_Speed?0#?"? _unitsH"ft/sec??d?'Tempe@(ureA(Process_Area??68SX?!F? Perc@]age0_MDIHKTc54?' ?3expectedRes?ult " ?J2?c68:C70??d??Rc72?LJd "?@c75@6O?(89:Cl91?ddjs9?3?m?n96?7?k110:Cl11I!?7d??11iS!P! ?/ = H?#gFalsyPuEn?y?c '=???7??#'\&?, L?.?"C?260")cP`#??c!'?!"?'"??W"A7?ga@x?y'' &e?/d1?j??K!@= ??'??? # ?T??6??<84?e?W?85P:306l3?3`07:32???3`29:35?s3`51:37=xc3`73:39?S3`95:41?C4`17:43?34?4??34618:48?#S'I f )?g The߰5'?`=?7???+??9?0?2(??1?2?2(??3?4?2(??R7?2(?8?9)?2(4Й41k 2?3 $4??5 1590 ??-?+?hE??????>10???8?????G0??J??!e??y2r????'?Q?EVS??wIfs 7?? (`_ _ _ _ G?? -0? ? ? 5 ?3 ??)?֭/?????ɱ9????C??H*?q?]__P??!?q???"?46?C?o??ָ?9??t???C?hϻ?pϻ?/?x}O?tèO?5?O?_?o6n?ť?sO?O?lc?O?O?O?O?"O????$? O?DyL????tHc0_A?M7??D@etails??O?n ???s?????&o?!?c?C? step` = 10?(' Dim ?As Integer?,@rMsg H?Stringb`rndxAry(20)HVari?ant, . ?1 MaxJfocus jnum_selecti,onG?w=Wo?rksheet`[e?9?r?7= "A7" ?Applica4.Enable@Events?False?Scr@eenUpdn~g??A ????'?#>*?Set |?= A?veS?| ?=?.Range("C260?").Valu?2?' )G'2Ċ?H?A~1)@;"27`1:282?Q?2??93:304?3?315:32 6?4?37:348?5?59:(370?6?81(:39?"7?40P3:41?"8?2P5:43?"9?4?7:45?"1@????469:48#?RDR?Mg.Unprot?? (glob_?_pass word)?FoFr?@? To s*? 1 '+ 1? ?eRows(?]??))??tire@?.Hiddenj?Not _en 1?NexciIL.Pvr~d 9dG?O?n)?.SBy? ?10??c?aTr?W?Nq?exit_sub :? E? Sub? err?? B?g?,??st?? DError. tc0_cmd_M7 ?>ow?2eCalcDetails_C??k2. in bB:" & ?Me.Name ?". atB?=?%_?!@& vb0CrLf!? N o.?`.Num8bercaaDe`scrip???'ׅ??ac1????'A`?no?E? ??BoxD,@OKOnly,$ "`orGo@c%; On: ? #C;End?= Priv8ate?)2clHear?s2(? r? a????\?6xH???c?4:??6???@z?kA?8 @??0d8688?V9?0 T?d30P 31Vd_312:\C3?V?53P3L32u33?3? 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VBAProjectSheet1Sheet2Sheet3Sheet4Sheet5Sheet6Sheet7Sheet25Sheet17Sheet27Sheet11Sheet12Sheet23Sheet14Sheet16Sheet8Sheet18Sheet35Sheet28Sheet31Module1 ThisWorkbookSheet10Sheet21Sheet26Sheet13Sheet9Sheet15??Fget_diffusivity_m2secHC:\Program Files (x86)\Common Files\Microsoft Shared\VBA\VBA7.1\VBE7.DLLVBA ????? ?0?F?C:\Program Files (x86)\Microsoft Office\root\Office16\EXCEL.EXEExcel ???? 9?@0?FC:\Windows\SysWOW64\stdole2.tlbstdole 1????Y?PL??-?[???D?REC:\Program Files (x86)\Common Files\Microsoft Shared\OFFICE16\MSO.DLLOffice ????9?`?.E???.`?M ?C:\WINDOWS\SysWOW64\FM20.DLLMSForms aa??p??u???M????f[9C:\Users\AVANHO~1\AppData\Local\Temp\Excel8.0\MSForms.exd A ai ?? PSRAget_HgVaporPress_mmHgF?Fconvert_temp_to_C disableEvent EnableEventRenameMSFormsFiles RenameFileCheckFileExist DeleteFile ??F?~?Q?{H@?????2??F!????cJ??I#ţ?D?FWorkbookWorkbook_BeforeCloseWorkbook_BeforeSaveWorkbook_Open @ A1 Overview??F SelectVisible LError. Hide_all_but_A1_sheet. at step=   Err no=?fĤ?I?x?8'M7 Binding Agent'!m7_calc1_Temperature_of_Process_Area_units$'M7 Binding Agent'!m7_calc10_result#'M7 Binding Agent'!m7_calc2_result#'M7 Binding Agent'!m7_calc3_result#'M7 Binding Agent'!m7_calc4_result#'M7 Binding Agent'!m7_calc5_result#'M7 Binding Agent'!m7_calc6_result#'M7 Binding Agent'!m7_calc7_result#'M7 Binding Agent'!m7_calc8_result#'M7 Binding Agent'!m7_calc9_result!'M7 Binding Agent'!m7_grandtotal$'M7 Binding Agent'!m7_num_selection('M7 Binding Agent'!m7_tpill_input_units'M7 Binding Agent'!m7_tspill#'M7 Binding Agent'!m7_tspill_inputm8_calc1_Airflow_Speedm8_calc1_Airflow_Speed_unitsm8_calc1_Aspillm8_calc1_Duration_of_spillm8_calc1_expectedResultm8_calc1_Percentage_TDIm8_calc1_result%m8_calc1_Temperature_of_Process_Area+m8_calc1_Temperature_of_Process_Area_unitsm8_calc10_resultm8_calc2_resultm8_calc3_resultm8_calc4_resultm8_calc5_resultm8_calc6_resultm8_calc7_resultm8_calc8_resultm8_calc9_resultm8_grandtotalm8_num_selectionm8_tpill_input_units m8_tspillm8_tspill_inputm9_calc1_eff_factorm9_calc1_totweightmdim9_grand_totalm9_num_selection)'M8a Spray Coating_Oven'!m9a_calc1_Cform2'M8a Spray Coating_Oven'!m9a_calc1_expectedResult8'M8a Spray Coating_Oven'!m9a_calc1_number_of_containers7'M8a Spray Coating_Oven'!m9a_calc1_Process_Temperature='M8a Spray Coating_Oven'!m9a_calc1_Process_Temperature_units*'M8a Spray Coating_Oven'!m9a_calc1_resultI'M8a Spray Coating_Oven'!m9a_calc1_TDI_ratio_in_the_isocyanate_feedstock('M8a Spray Coating_Oven'!m9a_calc1_Vair.'M8a Spray Coating_Oven'!m9a_calc1_vair_input4'M8a Spray Coating_Oven'!m9a_calc1_vair_input_units+'M8a Spray Coating_Oven'!m9a_calc10_result*'M8a Spray Coating_Oven'!m9a_calc2_result*'M8a Spray Coating_Oven'!m9a_calc3_result*'M8a Spray Coating_Oven'!m9a_calc4_result*'M8a Spray Coating_Oven'!m9a_calc5_result*'M8a Spray Coating_Oven'!m9a_calc6_result*'M8a Spray Coating_Oven'!m9a_calc7_result*'M8a Spray Coating_Oven'!m9a_calc8_result*'M8a Spray Coating_Oven'!m9a_calc9_result('M8a Spray Coating_Oven'!m9a_grandtotal+'M8b Spray Coating_Air Dry'!m9a_grandtotal+'M8a Spray Coating_Oven'!m9a_num_selection$'M8a Spray Coating_Oven'!m9a_tspray4'M8b Spray Coating_Air Dry'!m9b_calc1_Airflow_Speed:'M8b Spray Coating_Air Dry'!m9b_calc1_Airflow_Speed_units-'M8b Spray Coating_Air Dry'!m9b_calc1_Aspray8'M8b Spray Coating_Air Dry'!m9b_calc1_Duration_of_spray5'M8b Spray Coating_Air Dry'!m9b_calc1_expectedResult5'M8b Spray Coating_Air Dry'!m9b_calc1_Percentage_TDI-'M8b Spray Coating_Air Dry'!m9b_calc1_result='M8b Spray Coating_Air Dry'!m9b_calc1_Temperature_of_Air_DryC'M8b Spray Coating_Air Dry'!m9b_calc1_Temperature_of_Air_Dry_units.'M8b Spray Coating_Air Dry'!m9b_calc10_result-'M8b Spray Coating_Air Dry'!m9b_calc2_result-'M8b Spray Coating_Air Dry'!m9b_calc3_result-'M8b Spray Coating_Air Dry'!m9b_calc4_result-'M8b Spray Coating_Air Dry'!m9b_calc5_result-'M8b Spray Coating_Air Dry'!m9b_calc6_result-'M8b Spray Coating_Air Dry'!m9b_calc7_result-'M8b Spray Coating_Air Dry'!m9b_calc8_result-'M8b Spray Coating_Air Dry'!m9b_calc9_result+'M8b Spray Coating_Air Dry'!m9b_grandtotal.'M8b Spray Coating_Air Dry'!m9b_num_selection''M8b Spray Coating_Air Dry?? ??՜.??+,??D??՜.??+,?? +?* PXh px??? ?*?Berty . 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RecipientsReceivedTimeFrom?A?,?YK????Hu'A4 Guidance'!A1Ye'M8b Spray Coating_Air Dry'!A14'M8a Spray Coating_Oven'!A1JO'M8 Spray Coating'!A1G'M7 Spill'!A1PG!'M3c Fugitive SV is not zero'!A1J 'M3b Fugitive SV is Zero'!A1=u'M3a Fugitive no SV'!A1t'M6S Exhaust Air_Saturated'!A1T!'M6 Exhaust Air_Measured'!A1??????????????????????????????????????????????????????????????????????????????????????????????????????????????????????????????????????????????????????????????????????????????????????????????????????????????????????????????????????????????????????????????????????????????????????????????????????????????????????????????????????????????????????????????????????????????????????????????????????????????????????????????????????'M5a Open Process'!A1A'M5 Open Process Overview'!A1q!'M4b Enclosed Process_Volume'!A1{!'M4a Enclosed Process_Weight'!A19"'M4 Enclosed Process_Overview'!A1RF 'S1 Emissions Summary'!A1YK 'A4 Guidance'!A1M 'R2 Reference Tables'!A1_F 'R1 Reference Lookups'!A1;B!'M3 Fugitive_Equipment Leaks'!A1x!'M2 Fugitive_Monitoring Data'!A1JW'M1 Tank'!A1JC'A1 Overview'!B9D'A3 Links'!A1ZV'A2 Glossary'!A1RF'S1 Emissions Summary'!A1M'R2 Reference Tables'!A1_F'R1 Reference Lookups'!A1JC'A1 Overview'!B9fG6http://www.americanchemistry.com/s_plastics/index.aspJC'A1 Overview'!B9K"http://www.americanchemistry.com/JC'A1 Overview'!B9JC'A1 Overview'!B9JC'A1 Overview'!B9PG????N?!'M3c Fugitive SV is not zero'!A1J ????Q?'M3b Fugitive SV is Zero'!A1=u????R?'M3a Fugitive no SV'!A1JC'A1 Overview'!B9IB?????!'M3 Fugitive-Equipment Leaks'!A1;B?????!'M3 Fugitive_Equipment Leaks'!A1JC'A1 Overview'!B9IB?????!'M3 Fugitive-Equipment Leaks'!A1;B?????!'M3 Fugitive_Equipment Leaks'!A1JC'A1 Overview'!B9IB?????!'M3 Fugitive-Equipment Leaks'!A1;B?????!'M3 Fugitive_Equipment Leaks'!A1JC 'A1 Overview'!B9{??????!'M4a Enclosed Process_Weight'!A1q??????!'M4b Enclosed Process_Volume'!A1JC 'A1 Overview'!B9K????ِ"'M4 Enclosed Process-Overview'!A19????ې"'M4 Enclosed Process_Overview'!A1JC 'A1 Overview'!B9K?????"'M4 Enclosed Process-Overview'!A19?????"'M4 Enclosed Process_Overview'!A1JC 'A1 Overview'!B9?????'M5a Open Process'!A1?????'M5a Open Process'!A1JC'A1 Overview'!B9IB?????!'M3 Fugitive-Equipment Leaks'!A1A?????'M5 Open Process Overview'!A1JC'A1 Overview'!B9K????٠"'M4 Enclosed Process-Overview'!A1A????۠'M5 Open Process Overview'!A1JC'A1 Overview'!B9?????'M5a Open Process'!A1t?????'M6S Exhaust Air_Saturated'!A1JC'A1 Overview'!B9K?????"'M4 Enclosed Process-Overview'!A1T!?????'M6 Exhaust Air_Measured'!A1JC'A1 Overview'!B9JC'A1 Overview'!B9JC'A1 Overview'!B9JC'A1 Overview'!B9K?????"'M4 Enclosed Process-Overview'!A1KO?????'M9 Spray Coating'!A1JC'A1 Overview'!B9IB????ٴ!'M3 Fugitive-Equipment Leaks'!A1KO????۴'M9 Spray Coating'!A1JC'A1 Overview'!B9*e'M9b Spray Coating-Air Dry'!A14'M9a Spray Coating_Oven'!A1T!'M6 Exhaust Air_Measured'!A1PG!'M3c Fugitive SV is not zero'!A1J 'M3b Fugitive SV is Zero'!A1=u'M3a Fugitive no SV'!A1t'M6S Exhaust Air_Saturated'!A1*e'M9b Spray Coating-Air Dry'!A14'M9a Spray Coating_Oven'!A1KO'M9 Spray Coating'!A1H'M8 Spill'!A1'M5a Open Process'!A1A'M5 Open Process Overview'!A1q!'M4b Enclosed Process_Volume'!A1  !'M4a Enclosed Process-Weight'!A19 "'M4 Enclosed Process_Overview'!A1RF 'S1 Emissions Summary'!A1YK 'A4 Guidance'!A1M'R2 Reference Tables'!A1_F'R1 Reference Lookups'!A1IB!'M3 Fugitive-Equipment Leaks'!A1 !'M2 Fugitive-Monitoring Data'!A1JW'M1 Tank'!A1JC'A1 Overview'!B9D'A3 Links'!A1ZV'A2 Glossary'!A1IK'A1 Overview'!A1IK'A1 Overview'!A1JC'A1 Overview'!B9CompObj ???? l?????????????????????????????????????? ???? ?F Microsoft Excel 2003 WorksheetBiff8Excel.Sheet.8?9?q> This value indicates the number of saves or revisions. 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