% Exported from MKS Knowledge Base: MKS Core Knowledge Base - Work.mkskbd % Exported on Mar 23, 2020 at 23:39:07 classdef MatlabChemicals01 % Physical property values properties % Physical properties: temperature dependent coefficient maps mksDensityLiquidCoefficients = containers.Map; % kg-mol/m3 mksDensitySolidCoefficients = containers.Map; % kg-mol/m3 mksEnthalpyVaporizationCoefficients = containers.Map; % J/kg-mol mksIsobaricHeatCapacityLiquidCoefficients = containers.Map; % J/kg-mol K mksIsobaricHeatCapacitySolidCoefficients = containers.Map; % J/kg-mol K mksIsobaricHeatCapacityVaporCoefficients = containers.Map; % J/kg-mol K mksSurfaceTensionLiquidCoefficients = containers.Map; % N/m mksThermalConductivityLiquidCoefficients = containers.Map; % W/m K mksThermalConductivityVaporCoefficients = containers.Map; % W/m K mksVaporPressureLiquidCoefficients = containers.Map; % Pa mksViscosityLiquidCoefficients = containers.Map; % Pa s mksViscosityVaporCoefficients = containers.Map; % Pa s % Physical properties: constant property maps mksAcentricFactorValues = containers.Map; % - - - mksBoilingPointValues = containers.Map; % K mksCriticalCompressibilityValues = containers.Map; % - - - mksCriticalPressureValues = containers.Map; % Pa mksCriticalTemperatureValues = containers.Map; % K mksCriticalVolumeValues = containers.Map; % m3/kg-mol mksDipoleMomentValues = containers.Map; % C m mksEnthalpyCombustion298Values = containers.Map; % J/kg-mol mksEnthalpyFormationVapor298Values = containers.Map; % J/kg-mol mksEnthalpyFusionTmValues = containers.Map; % J/kg-mol mksEnthalpyVaporizationTbValues = containers.Map; % J/kg-mol mksFlammabilityLimitLowerValues = containers.Map; % - - - mksFlammabilityLimitUpperValues = containers.Map; % - - - mksFlashPointClosedCupValues = containers.Map; % K mksGibbsEnergyFormationVapor298Values = containers.Map; % J/kg-mol mksMeltingPointValues = containers.Map; % K mksMolecularWeightValues = containers.Map; % - - - mksRadiusGyrationValues = containers.Map; % m mksSolubilityParameterTotalValues = containers.Map; % (J/m3)^1/2 mksRefractiveIndexLiquid293Values = containers.Map; % - - - mksTriplePointTemperatureValues = containers.Map; % K mksTriplePointPressureValues = containers.Map; % Pa mksAbsoluteEntropy298Values = containers.Map; % J/kg-mol K mksAutoIgnitionTemperatureValues = containers.Map; % K end methods function object = MatlabChemicals01(names) % 1,1-Diacetoxyethane object.mksDensityLiquidCoefficients('1,1-Diacetoxyethane') = [1.30474338934314, 0.350989248106625, 620.392297195485, 0.636130296409207]; object.mksEnthalpyVaporizationCoefficients('1,1-Diacetoxyethane') = [69755462.0049579, 0.0633190921282753, 0.370293001395]; object.mksIsobaricHeatCapacityLiquidCoefficients('1,1-Diacetoxyethane') = [5633201.85425204, -63488.5274606751, 276.232344140056, -0.524858894616835, 0.000369400470939413]; object.mksIsobaricHeatCapacitySolidCoefficients('1,1-Diacetoxyethane') = [13324.0227482396, 778.933356094931, -0.763699170162166, 0.00106015051003687, -6.93753154893566E-07]; object.mksIsobaricHeatCapacityVaporCoefficients('1,1-Diacetoxyethane') = [81631.6313392588, 173662.058254189, 545.898849066223, 123293.333457826, 839.215363937521]; object.mksSurfaceTensionLiquidCoefficients('1,1-Diacetoxyethane') = [0.0699326146231378, 1.22222222222223, -7.2600665283713E-15]; object.mksThermalConductivityLiquidCoefficients('1,1-Diacetoxyethane') = [0.210881058951656, -0.000119189580053281, -4.59870159864263E-07, 8.41765186909429E-10, -8.03872601077463E-13]; object.mksThermalConductivityVaporCoefficients('1,1-Diacetoxyethane') = [104.250927636844, 0.478971817127662, 48287702.8607014, 2922736642.12453]; object.mksVaporPressureLiquidCoefficients('1,1-Diacetoxyethane') = [379.697211818516, -20423.9903844496, 0, 0, -54.6440551428089, 5.54981889743181E-05, 2]; object.mksViscosityLiquidCoefficients('1,1-Diacetoxyethane') = [-11.6332637207781, 1510.99999999988, -4.88906136323888E-13, 6.39366990238917E-19]; object.mksViscosityVaporCoefficients('1,1-Diacetoxyethane') = [4.58594908547668E-06, 0.360925236395957, 1771.79906191718, -134178.130108797]; object.mksAcentricFactorValues('1,1-Diacetoxyethane') = 0.607502950416091; object.mksBoilingPointValues('1,1-Diacetoxyethane') = 442.15; object.mksCriticalCompressibilityValues('1,1-Diacetoxyethane') = 0.241239963060729; object.mksCriticalPressureValues('1,1-Diacetoxyethane') = 2970000; object.mksCriticalTemperatureValues('1,1-Diacetoxyethane') = 618.2; object.mksCriticalVolumeValues('1,1-Diacetoxyethane') = 0.4175; object.mksEnthalpyCombustion298Values('1,1-Diacetoxyethane') = -2923428412.32877; object.mksEnthalpyFormationVapor298Values('1,1-Diacetoxyethane') = -807010000; object.mksEnthalpyFusionTmValues('1,1-Diacetoxyethane') = 16511000; object.mksEnthalpyVaporizationTbValues('1,1-Diacetoxyethane') = 43473143.5106541; object.mksFlammabilityLimitLowerValues('1,1-Diacetoxyethane') = 1.499700059988; object.mksFlammabilityLimitUpperValues('1,1-Diacetoxyethane') = 8.52199100863241; object.mksFlashPointClosedCupValues('1,1-Diacetoxyethane') = 336.377373162191; object.mksGibbsEnergyFormationVapor298Values('1,1-Diacetoxyethane') = -609130000; object.mksMeltingPointValues('1,1-Diacetoxyethane') = 292; object.mksMolecularWeightValues('1,1-Diacetoxyethane') = 146.143; object.mksRadiusGyrationValues('1,1-Diacetoxyethane') = 4.481E-10; object.mksSolubilityParameterTotalValues('1,1-Diacetoxyethane') = 20606.8553093886; object.mksAutoIgnitionTemperatureValues('1,1-Diacetoxyethane') = 753.377271617868; if( nargin > 0 ) names{end+1} = '1,1-Diacetoxyethane'; end % 1,1-Dichloro-1-fluoroethane object.mksDensityLiquidCoefficients('1,1-Dichloro-1-fluoroethane') = [1.72528951900044, 0.348707186956578, 387.663488546969, 0.220509477514913]; object.mksEnthalpyVaporizationCoefficients('1,1-Dichloro-1-fluoroethane') = [33874891.1492029, 0.142047136924937, 0.230373988682482]; object.mksIsobaricHeatCapacityLiquidCoefficients('1,1-Dichloro-1-fluoroethane') = [625042.01803766, -9649.74617155142, 66.2503235060429, -0.195342554871073, 0.000211989537911884]; object.mksIsobaricHeatCapacitySolidCoefficients('1,1-Dichloro-1-fluoroethane') = [6382.92687561591, 685.424583884896, -1.23092311804312, 0.0031211314938705, -3.72039352957528E-06]; object.mksIsobaricHeatCapacityVaporCoefficients('1,1-Dichloro-1-fluoroethane') = [49016.5268289939, 112970.059233073, 1082.44637608699, 92445.0352644613, 485.412848271534]; object.mksSurfaceTensionLiquidCoefficients('1,1-Dichloro-1-fluoroethane') = [0.068304, 1.2878, 2.66301352358491E-15]; object.mksThermalConductivityLiquidCoefficients('1,1-Dichloro-1-fluoroethane') = [0.173450000000005, -0.000264390000000081, 5.4630302353239E-19, -1.62856607179312E-21, 1.80912561962197E-24]; object.mksThermalConductivityVaporCoefficients('1,1-Dichloro-1-fluoroethane') = [106.140945831383, 0.512911085646568, 45620255.9398909, 3884845520.08278]; object.mksVaporPressureLiquidCoefficients('1,1-Dichloro-1-fluoroethane') = [101.717045435144, -5931.76633306753, 0, 0, -12.7460009210663, 2.338367338417E-05, 2]; object.mksViscosityLiquidCoefficients('1,1-Dichloro-1-fluoroethane') = [-109.74373461139, 3397.25014268244, 16.5647883997953, -4.52673132729129E-05]; object.mksViscosityVaporCoefficients('1,1-Dichloro-1-fluoroethane') = [5.62121292867057E-06, 0.370420757800203, 1291.57123322992, -74008.4639198777]; object.mksAcentricFactorValues('1,1-Dichloro-1-fluoroethane') = 0.230474745605102; object.mksBoilingPointValues('1,1-Dichloro-1-fluoroethane') = 305.15; object.mksCriticalCompressibilityValues('1,1-Dichloro-1-fluoroethane') = 0.269; object.mksCriticalPressureValues('1,1-Dichloro-1-fluoroethane') = 4200000; object.mksCriticalTemperatureValues('1,1-Dichloro-1-fluoroethane') = 477.5; object.mksCriticalVolumeValues('1,1-Dichloro-1-fluoroethane') = 0.254; object.mksDipoleMomentValues('1,1-Dichloro-1-fluoroethane') = 6.718E-30; object.mksEnthalpyCombustion298Values('1,1-Dichloro-1-fluoroethane') = -898389529.771182; object.mksEnthalpyFormationVapor298Values('1,1-Dichloro-1-fluoroethane') = -320950000; object.mksEnthalpyFusionTmValues('1,1-Dichloro-1-fluoroethane') = 4996000; object.mksEnthalpyVaporizationTbValues('1,1-Dichloro-1-fluoroethane') = 25863161.1311378; object.mksFlammabilityLimitLowerValues('1,1-Dichloro-1-fluoroethane') = 5.41711809317443; object.mksFlammabilityLimitUpperValues('1,1-Dichloro-1-fluoroethane') = 31.7904734120653; object.mksFlashPointClosedCupValues('1,1-Dichloro-1-fluoroethane') = 242.057198811329; object.mksGibbsEnergyFormationVapor298Values('1,1-Dichloro-1-fluoroethane') = -235460000; object.mksMeltingPointValues('1,1-Dichloro-1-fluoroethane') = 169.65; object.mksMolecularWeightValues('1,1-Dichloro-1-fluoroethane') = 116.95; object.mksRadiusGyrationValues('1,1-Dichloro-1-fluoroethane') = 3.214E-10; object.mksSolubilityParameterTotalValues('1,1-Dichloro-1-fluoroethane') = 15663.6251662914; object.mksAutoIgnitionTemperatureValues('1,1-Dichloro-1-fluoroethane') = 854.087233858697; if( nargin > 0 ) names{end+1} = '1,1-Dichloro-1-fluoroethane'; end % 1,1-Dichloroethane object.mksDensityLiquidCoefficients('1,1-Dichloroethane') = [1.77745567601645, 0.337613499767176, 485.642018594527, 0.310788835835871]; object.mksEnthalpyVaporizationCoefficients('1,1-Dichloroethane') = [28639909.5613771, -1.00776927745961, 1.60739468724681]; object.mksIsobaricHeatCapacityLiquidCoefficients('1,1-Dichloroethane') = [359961.514920409, -3861.62351989225, 22.8454048255596, -0.0592153842477108, 5.77605305434035E-05]; object.mksIsobaricHeatCapacitySolidCoefficients('1,1-Dichloroethane') = [6083.69663330967, 624.347434824847, -1.07191393013323, 0.00259923167966622, -2.9639087597329E-06]; object.mksIsobaricHeatCapacityVaporCoefficients('1,1-Dichloroethane') = [50166.9913000661, 98987.118633849, 1140.38967488511, 72559.8122739284, 555.344174048734]; object.mksSurfaceTensionLiquidCoefficients('1,1-Dichloroethane') = [0.0687042535541448, 1.01535865521271, 0.356104044765366]; object.mksThermalConductivityLiquidCoefficients('1,1-Dichloroethane') = [1.40070481909232, -0.0195891811081238, 0.00011445785583565, -2.98258101330469E-07, 2.88657872961576E-10]; object.mksThermalConductivityVaporCoefficients('1,1-Dichloroethane') = [107.272875459674, 0.507871440463645, 44169213.6429041, 5089882187.93051]; object.mksVaporPressureLiquidCoefficients('1,1-Dichloroethane') = [133.397517959929, -7501.94254327128, 0, 0, -17.6321905271795, 2.89714867495797E-05, 2]; object.mksViscosityLiquidCoefficients('1,1-Dichloroethane') = [23.9366291541224, -40.9308679429116, -5.74130652308197, 1.39299355096245E-05]; object.mksViscosityVaporCoefficients('1,1-Dichloroethane') = [5.38380823053037E-06, 0.354018071647348, 1133.80681233141, -54658.8019644489]; object.mksAcentricFactorValues('1,1-Dichloroethane') = 0.24; object.mksBoilingPointValues('1,1-Dichloroethane') = 330.45; object.mksCriticalCompressibilityValues('1,1-Dichloroethane') = 0.275; object.mksCriticalPressureValues('1,1-Dichloroethane') = 5070000; object.mksCriticalTemperatureValues('1,1-Dichloroethane') = 523; object.mksCriticalVolumeValues('1,1-Dichloroethane') = 0.236; object.mksDipoleMomentValues('1,1-Dichloroethane') = 6.8714184E-30; object.mksEnthalpyCombustion298Values('1,1-Dichloroethane') = -1105157090.51485; object.mksEnthalpyFormationVapor298Values('1,1-Dichloroethane') = -121370000; object.mksEnthalpyFusionTmValues('1,1-Dichloroethane') = 7870000; object.mksEnthalpyVaporizationTbValues('1,1-Dichloroethane') = 29144089.5898493; object.mksFlammabilityLimitLowerValues('1,1-Dichloroethane') = 5.4; object.mksFlammabilityLimitUpperValues('1,1-Dichloroethane') = 11.4; object.mksFlashPointClosedCupValues('1,1-Dichloroethane') = 256.483333333333; object.mksGibbsEnergyFormationVapor298Values('1,1-Dichloroethane') = -45930000; object.mksMeltingPointValues('1,1-Dichloroethane') = 176.18; object.mksMolecularWeightValues('1,1-Dichloroethane') = 98.959; object.mksRadiusGyrationValues('1,1-Dichloroethane') = 3.095E-10; object.mksSolubilityParameterTotalValues('1,1-Dichloroethane') = 18300; object.mksAutoIgnitionTemperatureValues('1,1-Dichloroethane') = 730.927777777778; if( nargin > 0 ) names{end+1} = '1,1-Dichloroethane'; end % 1,1-Diethoxyethane object.mksDensityLiquidCoefficients('1,1-Diethoxyethane') = [1.31014783233777, 0.427306900151765, 3688982205559.36, 29171210.5579749]; object.mksEnthalpyVaporizationCoefficients('1,1-Diethoxyethane') = [51703937.8740776, 0.321908696744912, 0.0344858351102686]; object.mksIsobaricHeatCapacityLiquidCoefficients('1,1-Diethoxyethane') = [259748.615348793, 583.27997954024, -11.4857214373726, 0.0531681149871019, -7.01394586604882E-05]; object.mksIsobaricHeatCapacitySolidCoefficients('1,1-Diethoxyethane') = [9083.0363533549, 951.71869764853, -1.66800312089414, 0.00412831929526907, -4.80421275011117E-06]; object.mksIsobaricHeatCapacityVaporCoefficients('1,1-Diethoxyethane') = [59822.9237274448, 256631.751200092, 628.680746738561, 83706.4715226976, 350.289436380839]; object.mksSurfaceTensionLiquidCoefficients('1,1-Diethoxyethane') = [0.0827739944496734, 2.02555704542759, -0.788256354113593]; object.mksThermalConductivityLiquidCoefficients('1,1-Diethoxyethane') = [0.222426388937074, -0.000212343344249154, -2.6453795694006E-07, 5.24125489899391E-10, -7.91792935613986E-13]; object.mksThermalConductivityVaporCoefficients('1,1-Diethoxyethane') = [103.170457839646, 0.515222905409628, 48346307.7196197, 2505836405.05864]; object.mksVaporPressureLiquidCoefficients('1,1-Diethoxyethane') = [-537.461819773146, 15704.3247152401, 0, 0, 88.5667042445431, -0.00012685049370743, 2]; object.mksViscosityLiquidCoefficients('1,1-Diethoxyethane') = [-136.085739418338, 4938.33691273811, 20.1936071221594, -3.71231672893733E-05]; object.mksViscosityVaporCoefficients('1,1-Diethoxyethane') = [4.69447721751552E-06, 0.352308183427672, 1619.78839772676, -104724.244571622]; object.mksAcentricFactorValues('1,1-Diethoxyethane') = 0.475342138753252; object.mksBoilingPointValues('1,1-Diethoxyethane') = 376.75; object.mksCriticalCompressibilityValues('1,1-Diethoxyethane') = 0.287947283920089; object.mksCriticalPressureValues('1,1-Diethoxyethane') = 3220000; object.mksCriticalTemperatureValues('1,1-Diethoxyethane') = 540; object.mksCriticalVolumeValues('1,1-Diethoxyethane') = 0.4015; object.mksDipoleMomentValues('1,1-Diethoxyethane') = 3.6025E-30; object.mksEnthalpyCombustion298Values('1,1-Diethoxyethane') = -3870460000; object.mksEnthalpyFormationVapor298Values('1,1-Diethoxyethane') = -453590000; object.mksEnthalpyFusionTmValues('1,1-Diethoxyethane') = 10149000; object.mksEnthalpyVaporizationTbValues('1,1-Diethoxyethane') = 35693796.7383224; object.mksFlammabilityLimitLowerValues('1,1-Diethoxyethane') = 1.6; object.mksFlammabilityLimitUpperValues('1,1-Diethoxyethane') = 10.4; object.mksFlashPointClosedCupValues('1,1-Diethoxyethane') = 252.594444444444; object.mksGibbsEnergyFormationVapor298Values('1,1-Diethoxyethane') = -198390000; object.mksMeltingPointValues('1,1-Diethoxyethane') = 173.15; object.mksMolecularWeightValues('1,1-Diethoxyethane') = 118.176; object.mksRadiusGyrationValues('1,1-Diethoxyethane') = 4.329E-10; object.mksSolubilityParameterTotalValues('1,1-Diethoxyethane') = 16000.7172347083; object.mksAutoIgnitionTemperatureValues('1,1-Diethoxyethane') = 503.15; if( nargin > 0 ) names{end+1} = '1,1-Diethoxyethane'; end end function y = mksDensityLiquid(object, chemical, temp) % Equation: Y = A / B^(1 + (1 - T/C)^D) % Property: Density, Liquid - f(T) % Units: kg-mol/m3 params = object.mksDensityLiquidCoefficients(chemical); term1 = (1.0 - temp / params(3)) ^ params(4); term2 = params(2) ^ (1.0 + term1); y = params(1) / term2; end function y = mksDensitySolid(object, chemical, temp) % Equation: Y = A + BT % Property: Density, Solid - f(T) % Units: kg-mol/m3 params = object.mksDensitySolidCoefficients(chemical); y = params(1) + params(2) * temp; end function y = mksEnthalpyVaporization(object, chemical, temp) % Equation: Y = A(1 - Tr)^(B + CTr) % Property: Enthalpy of Vaporization - f(T) % Units: J/kg-mol params = object.mksEnthalpyVaporizationCoefficients(chemical); tc = mksCriticalTemperature(chemical); term1 = params(2) + params(3) * (temp / tc); term2 = (1.0 - temp / tc) ^ term1; y = params(1) / term2; end function y = mksIsobaricHeatCapacityLiquid(object, chemical, temp) % Equation: Y = A + BT + CT^2 + DT^3 + ET^4 % Property: Heat Capacity - Isobaric, Liquid - f(T) % Units: J/kg-mol K params = object.mksIsobaricHeatCapacityLiquidCoefficients(chemical); term1 = params(1) + params(2) * temp + params(3) * temp ^ 2.0; term2 = params(4) * temp ^ 3.0 + params(5) * temp ^ 4.0; y = term1 + term2; end function y = mksIsobaricHeatCapacitySolid(object, chemical, temp) % Equation: Y = A + BT + CT^2 + DT^3 + ET^4 % Property: Heat Capacity - Isobaric, Solid - f(T) % Units: J/kg-mol K params = object.mksIsobaricHeatCapacitySolidCoefficients(chemical); term1 = params(1) + params(2) * temp + params(3) * temp ^ 2.0; term2 = params(4) * temp ^ 3.0 + params(5) * temp ^ 4.0; y = term1 + term2; end function y = mksIsobaricHeatCapacityVapor(object, chemical, temp) % Equation: Y = A + B(C/T/sinh(C/T))^2 + D(E/T/cosh(E/T))^2 % Property: Heat Capacity - Isobaric, Vapor - f(T) % Units: J/kg-mol K params = object.mksIsobaricHeatCapacityVaporCoefficients(chemical); term1 = params(3) / temp / sinh(params(3) / temp); term2 = params(5) / temp / cosh(params(5) / temp); term1 = params(2) * term1 ^ 2.0; term2 = params(4) * term2 ^ 2.0; y = params(1) + term1 + term2; end function y = mksSurfaceTensionLiquid(object, chemical, temp) % Equation: Y = A(1 - Tr)^(B + CTr) % Property: Surface Tension, Liquid - f(T) % Units: N/m params = object.mksSurfaceTensionLiquidCoefficients(chemical); tc = mksCriticalTemperature(chemical); term1 = params(2) + params(3) * (temp / tc); term2 = (1.0 - temp / tc) ^ term1; y = params(1) / term2; end function y = mksThermalConductivityLiquid(object, chemical, temp) % Equation: Y = A + BT + CT^2 + DT^3 + ET^4 % Property: Thermal Conductivity, Liquid - f(T) % Units: W/m K params = object.mksThermalConductivityLiquidCoefficients(chemical); term1 = params(1) + params(2) * temp + params(3) * temp ^ 2.0; term2 = params(4) * temp ^ 3.0 + params(5) * temp ^ 4.0; y = term1 + term2; end function y = mksThermalConductivityVapor(object, chemical, temp) % Equation: Y = A * T^B / (1 + C/T + D/T^2) % Property: Thermal Conductivity, Vapor - f(T) % Units: W/m K params = object.mksThermalConductivityVaporCoefficients(chemical); term1 = 1.0 + params(3) / temp + params(4) / temp ^ 2.0; term2 = params(1) * temp ^ params(2); y = term2 / term1; end function y = mksVaporPressureLiquid(object, chemical, temp) % Equation: Y = exp(A + B/T + ClnT + DT^2) % Property: Vapor Pressure, Liquid - f(T) % Units: Pa params = object.mksVaporPressureLiquidCoefficients(chemical); term1 = params(3) * log(temp) + params(4) * temp ^ 2.0; term2 = params(1) + params(2) / temp; y = exp(term1 + term2); end function y = mksViscosityLiquid(object, chemical, temp) % Equation: Y = exp(A + B/T + ClnT + DT^2) % Property: Viscosity, Liquid - f(T) % Units: Pa s params = object.mksViscosityLiquidCoefficients(chemical); term1 = params(3) * log(temp) + params(4) * temp ^ 2.0; term2 = params(1) + params(2) / temp; y = exp(term1 + term2); end function y = mksViscosityVapor(object, chemical, temp) % Equation: Y = A * T^B / (1 + C/T + D/T^2) % Property: Viscosity, Vapor - f(T) % Units: Pa s params = object.mksViscosityVaporCoefficients(chemical); term1 = 1.0 + params(3) / temp + params(4) / temp ^ 2.0; term2 = params(1) * temp ^ params(2); y = term2 / term1; end function y = mksAcentricFactor(object, chemical) % Property: Acentric Factor % Units: - - - y = object.mksAcentricFactorValues(chemical); end function y = mksBoilingPoint(object, chemical) % Property: Boiling Point % Units: K y = object.mksBoilingPointValues(chemical); end function y = mksCriticalCompressibility(object, chemical) % Property: Critical Compressibility % Units: - - - y = object.mksCriticalCompressibilityValues(chemical); end function y = mksCriticalPressure(object, chemical) % Property: Critical Pressure % Units: Pa y = object.mksCriticalPressureValues(chemical); end function y = mksCriticalTemperature(object, chemical) % Property: Critical Temperature % Units: K y = object.mksCriticalTemperatureValues(chemical); end function y = mksCriticalVolume(object, chemical) % Property: Critical Volume % Units: m3/kg-mol y = object.mksCriticalVolumeValues(chemical); end function y = mksDipoleMoment(object, chemical) % Property: Dipole Moment % Units: C m y = object.mksDipoleMomentValues(chemical); end function y = mksEnthalpyCombustion298(object, chemical) % Property: Enthalpy of Combustion at 298K % Units: J/kg-mol y = object.mksEnthalpyCombustion298Values(chemical); end function y = mksEnthalpyFormationVapor298(object, chemical) % Property: Enthalpy of Formation, Vapor at 298K % Units: J/kg-mol y = object.mksEnthalpyFormationVapor298Values(chemical); end function y = mksEnthalpyFusionTm(object, chemical) % Property: Enthalpy of Fusion at Tm % Units: J/kg-mol y = object.mksEnthalpyFusionTmValues(chemical); end function y = mksEnthalpyVaporizationTb(object, chemical) % Property: Enthalpy of Vaporization at Tb % Units: J/kg-mol y = object.mksEnthalpyVaporizationTbValues(chemical); end function y = mksFlammabilityLimitLower(object, chemical) % Property: Flammability Limit, Lower % Units: - - - y = object.mksFlammabilityLimitLowerValues(chemical); end function y = mksFlammabilityLimitUpper(object, chemical) % Property: Flammability Limit, Upper % Units: - - - y = object.mksFlammabilityLimitUpperValues(chemical); end function y = mksFlashPointClosedCup(object, chemical) % Property: Flash Point, Closed Cup % Units: K y = object.mksFlashPointClosedCupValues(chemical); end function y = mksGibbsEnergyFormationVapor298(object, chemical) % Property: Gibbs Energy of Formation, Vapor at 298K % Units: J/kg-mol y = object.mksGibbsEnergyFormationVapor298Values(chemical); end function y = mksMeltingPoint(object, chemical) % Property: Melting Point % Units: K y = object.mksMeltingPointValues(chemical); end function y = mksMolecularWeight(object, chemical) % Property: Molecular Weight % Units: - - - y = object.mksMolecularWeightValues(chemical); end function y = mksRadiusGyration(object, chemical) % Property: Radius of Gyration % Units: m y = object.mksRadiusGyrationValues(chemical); end function y = mksSolubilityParameterTotal(object, chemical) % Property: Solubility Parameter, Total % Units: (J/m3)^1/2 y = object.mksSolubilityParameterTotalValues(chemical); end function y = mksRefractiveIndexLiquid293(object, chemical) % Property: Refractive Index, Liquid at 293K % Units: - - - y = object.mksRefractiveIndexLiquid293Values(chemical); end function y = mksTriplePointTemperature(object, chemical) % Property: Triple Point, Temperature % Units: K y = object.mksTriplePointTemperatureValues(chemical); end function y = mksTriplePointPressure(object, chemical) % Property: Triple Point, Pressure % Units: Pa y = object.mksTriplePointPressureValues(chemical); end function y = mksAbsoluteEntropy298(object, chemical) % Property: Standard Entropy at 298K % Units: J/kg-mol K y = object.mksAbsoluteEntropy298Values(chemical); end function y = mksAutoIgnitionTemperature(object, chemical) % Property: Autoignition Temperature % Units: K y = object.mksAutoIgnitionTemperatureValues(chemical); end end end