% Exported from MKS Knowledge Base: MKS Core Knowledge Base - Internal.mkskbd
% Exported on Mar 27, 2020 at 23:00:37

classdef MatlabExportFile01
% 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 = MatlabExportFile01(names)

			% Acetic acid
			object.mksDensityLiquidCoefficients('Acetic acid') = [1.66839773685555, 0.31268322466212, 12105.6198119883, 0.310480748194666];
			object.mksEnthalpyVaporizationCoefficients('Acetic acid') = [72237843.9255362, 3.07430700203591, -3.04547030671635];
			object.mksIsobaricHeatCapacityLiquidCoefficients('Acetic acid') = [9505169.88055106, -115838.543666244, 534.076760240227, -1.09133945822137, 0.000835713172293383];
			object.mksIsobaricHeatCapacityVaporCoefficients('Acetic acid') = [42278.743632085, 86853.0573263708, 1184.41570107857, 76491.8062476673, 650.284267432542];
			object.mksSurfaceTensionLiquidCoefficients('Acetic acid') = [0.0604608845794949, 1.21298143305731, -0.139247919716381];
			object.mksThermalConductivityLiquidCoefficients('Acetic acid') = [98.0432624162591, -1.14739169933245, 0.00503256524225213, -9.78849588578339E-06, 7.12281620440983E-09];
			object.mksThermalConductivityVaporCoefficients('Acetic acid') = [112.929501818463, 0.535808893626915, 37153890.4691942, 9762702904.0262];
			object.mksVaporPressureLiquidCoefficients('Acetic acid') = [1507.23595842508, -59430.8097157552, 0, 0, -233.098770772025, 0.00031138561881513, 2];
			object.mksViscosityLiquidCoefficients('Acetic acid') = [-10.3498986854346, 1334.95770462879, -0.163861996769586, 2.91538890469596E-07];
			object.mksViscosityVaporCoefficients('Acetic acid') = [6.59111340144844E-06, 0.457442640421627, 2510.3434416608, 458109.27587508];
			object.mksAcentricFactorValues('Acetic acid') = 0.447;
			object.mksBoilingPointValues('Acetic acid') = 391.05;
			object.mksCriticalCompressibilityValues('Acetic acid') = 0.201;
			object.mksCriticalPressureValues('Acetic acid') = 5786000;
			object.mksCriticalTemperatureValues('Acetic acid') = 592.71;
			object.mksCriticalVolumeValues('Acetic acid') = 0.171;
			object.mksDipoleMomentValues('Acetic acid') = 5.8040136E-30;
			object.mksEnthalpyCombustion298Values('Acetic acid') = -874539680;
			object.mksEnthalpyFormationVapor298Values('Acetic acid') = -432800000;
			object.mksEnthalpyFusionTmValues('Acetic acid') = 11720000;
			object.mksEnthalpyVaporizationTbValues('Acetic acid') = 39443968.2291054;
			object.mksFlammabilityLimitLowerValues('Acetic acid') = 4;
			object.mksFlammabilityLimitUpperValues('Acetic acid') = 19.9;
			object.mksFlashPointClosedCupValues('Acetic acid') = 312.594444444444;
			object.mksGibbsEnergyFormationVapor298Values('Acetic acid') = -363540000;
			object.mksMeltingPointValues('Acetic acid') = 289.49;
			object.mksMolecularWeightValues('Acetic acid') = 60.053;
			object.mksRadiusGyrationValues('Acetic acid') = 2.61E-10;
			object.mksSolubilityParameterTotalValues('Acetic acid') = 26500;
			object.mksTriplePointTemperatureValues('Acetic acid') = 289.69;
			object.mksAutoIgnitionTemperatureValues('Acetic acid') = 737.038888888889;
			if( nargin > 0 )
				names{end+1} = 'Acetic acid';
			end

			% Cyclohexanol
			object.mksDensityLiquidCoefficients('Cyclohexanol') = [1.42067806459306, 0.400079452688862, 14747.7849473867, 0.0297864059745372];
			object.mksEnthalpyVaporizationCoefficients('Cyclohexanol') = [51314264.2514884, -1.00193625886766, 1.57523051637368];
			object.mksIsobaricHeatCapacityLiquidCoefficients('Cyclohexanol') = [237890.027184077, -920.744740874703, 4.67300325156414, -0.00779611373209328, 5.07146905085181E-06];
			object.mksIsobaricHeatCapacitySolidCoefficients('Cyclohexanol') = [42924.1415498149, 520.163250826149, -0.410284338590905, 0.000874837467922429, -6.77041699051413E-07];
			object.mksIsobaricHeatCapacityVaporCoefficients('Cyclohexanol') = [86483.3954332168, 185488.006977731, 707.64072080172, 147754.187707065, 1276.23513419275];
			object.mksSurfaceTensionLiquidCoefficients('Cyclohexanol') = [0.0654, 1.036, 5.88727809709422E-16];
			object.mksThermalConductivityVaporCoefficients('Cyclohexanol') = [111.968769520191, 0.524704734348881, 38881411.4606645, 9384333705.67113];
			object.mksVaporPressureLiquidCoefficients('Cyclohexanol') = [98.3437900471932, -10258.9389495473, 0, 0, -10.3947431651173, -2.10999132661764E-07, 2];
			object.mksViscosityLiquidCoefficients('Cyclohexanol') = [4692.57829261503, -177091.848299436, -734.023897880117, 0.000881293051710386];
			object.mksViscosityVaporCoefficients('Cyclohexanol') = [4.62282363049196E-06, 0.347034933642604, 1365.69573456995, -70889.7319846428];
			object.mksAcentricFactorValues('Cyclohexanol') = 0.528;
			object.mksBoilingPointValues('Cyclohexanol') = 434;
			object.mksCriticalCompressibilityValues('Cyclohexanol') = 0.254958234396769;
			object.mksCriticalPressureValues('Cyclohexanol') = 4260000;
			object.mksCriticalTemperatureValues('Cyclohexanol') = 650.1;
			object.mksCriticalVolumeValues('Cyclohexanol') = 0.3235;
			object.mksDipoleMomentValues('Cyclohexanol') = 6.2043E-30;
			object.mksEnthalpyCombustion298Values('Cyclohexanol') = -3726981680;
			object.mksEnthalpyFormationVapor298Values('Cyclohexanol') = -286200000;
			object.mksEnthalpyFusionTmValues('Cyclohexanol') = 7219000;
			object.mksEnthalpyVaporizationTbValues('Cyclohexanol') = 40739845.7462495;
			object.mksFlammabilityLimitLowerValues('Cyclohexanol') = 0.296359545797206;
			object.mksFlammabilityLimitUpperValues('Cyclohexanol') = 9.34447924922915;
			object.mksFlashPointClosedCupValues('Cyclohexanol') = 340.35;
			object.mksGibbsEnergyFormationVapor298Values('Cyclohexanol') = -98320000;
			object.mksMeltingPointValues('Cyclohexanol') = 296.6;
			object.mksMolecularWeightValues('Cyclohexanol') = 100.161;
			object.mksRadiusGyrationValues('Cyclohexanol') = 3.601E-10;
			object.mksSolubilityParameterTotalValues('Cyclohexanol') = 23672;
			object.mksAutoIgnitionTemperatureValues('Cyclohexanol') = 573.15;
			if( nargin > 0 )
				names{end+1} = 'Cyclohexanol';
			end

			% Ethanol
			object.mksDensityLiquidCoefficients('Ethanol') = [1.9026197591758, 0.2852661614003, 1229.83624712447, 1.0514887009673];
			object.mksEnthalpyVaporizationCoefficients('Ethanol') = [43829562.1651149, -0.458890296480571, 0.831397347741495];
			object.mksIsobaricHeatCapacityLiquidCoefficients('Ethanol') = [94560.0000000018, -56.2000000000289, -0.328999999999824, 0.00239799999999953, 4.66903008005322E-19];
			object.mksIsobaricHeatCapacitySolidCoefficients('Ethanol') = [8441.07715623169, 513.942186519769, -2.56766962756316, 0.00995233787046964, -1.50820352208727E-05];
			object.mksIsobaricHeatCapacityVaporCoefficients('Ethanol') = [45675.7146210464, 48276.9151622893, 1234.78311917767, 87682.7354528113, 328.915619665231];
			object.mksSurfaceTensionLiquidCoefficients('Ethanol') = [0.0350859103813713, 0.257514267871668, 0.487008443067949];
			object.mksThermalConductivityLiquidCoefficients('Ethanol') = [-0.165287018902558, 0.00656892992540505, -3.73380742885749E-05, 8.21688573392361E-08, -6.18105630417913E-11];
			object.mksThermalConductivityVaporCoefficients('Ethanol') = [116.195948775989, 0.537678253211774, 37887220.9232546, 3099924182.52362];
			object.mksVaporPressureLiquidCoefficients('Ethanol') = [127.025529446322, -8907.2627550231, 0, 0, -15.7525418366619, 1.77135890659281E-05, 2];
			object.mksViscosityLiquidCoefficients('Ethanol') = [-222.289150952618, 8488.51714376963, 33.7766818550241, -6.13052537185796E-05];
			object.mksViscosityVaporCoefficients('Ethanol') = [5.20868954634765E-06, 0.338081510358605, 1123.97034654581, -72001.4342428863];
			object.mksAcentricFactorValues('Ethanol') = 0.644;
			object.mksBoilingPointValues('Ethanol') = 351.44;
			object.mksCriticalCompressibilityValues('Ethanol') = 0.24;
			object.mksCriticalPressureValues('Ethanol') = 6137000;
			object.mksCriticalTemperatureValues('Ethanol') = 513.92;
			object.mksCriticalVolumeValues('Ethanol') = 0.167;
			object.mksDipoleMomentValues('Ethanol') = 5.6372316E-30;
			object.mksEnthalpyCombustion298Values('Ethanol') = -1367582240;
			object.mksEnthalpyFormationVapor298Values('Ethanol') = -235300000;
			object.mksEnthalpyFusionTmValues('Ethanol') = 4931000;
			object.mksEnthalpyVaporizationTbValues('Ethanol') = 39243423.9122667;
			object.mksFlammabilityLimitLowerValues('Ethanol') = 3.3;
			object.mksFlammabilityLimitUpperValues('Ethanol') = 19;
			object.mksFlashPointClosedCupValues('Ethanol') = 286.15;
			object.mksGibbsEnergyFormationVapor298Values('Ethanol') = -156450000;
			object.mksMeltingPointValues('Ethanol') = 159.05;
			object.mksMolecularWeightValues('Ethanol') = 46.069;
			object.mksRadiusGyrationValues('Ethanol') = 2.259E-10;
			object.mksSolubilityParameterTotalValues('Ethanol') = 26100;
			object.mksRefractiveIndexLiquid293Values('Ethanol') = 1.36139;
			object.mksAutoIgnitionTemperatureValues('Ethanol') = 635.927777777778;
			if( nargin > 0 )
				names{end+1} = 'Ethanol';
			end

			% Ethyl acetate
			object.mksDensityLiquidCoefficients('Ethyl acetate') = [1.54618283171595, 0.367480173691376, -2456.13039656214, -1.22132208694905];
			object.mksEnthalpyVaporizationCoefficients('Ethyl acetate') = [49330000, 0.3847, 3.35902448016327E-16];
			object.mksIsobaricHeatCapacityLiquidCoefficients('Ethyl acetate') = [-1016385.02996191, 18079.162507392, -101.840153680165, 0.249348366498623, -0.000222670071744547];
			object.mksIsobaricHeatCapacitySolidCoefficients('Ethyl acetate') = [24036.4053391303, 572.977515665775, -1.64023610762019, 0.00546368597441317, -6.80981138220961E-06];
			object.mksIsobaricHeatCapacityVaporCoefficients('Ethyl acetate') = [55143.226517813, 203293.88349885, 932.011890485183, 99193.5046774583, 393.974589132138];
			object.mksSurfaceTensionLiquidCoefficients('Ethyl acetate') = [0.067276804516297, 1.27631789004575, -0.0500830456912304];
			object.mksThermalConductivityLiquidCoefficients('Ethyl acetate') = [1.22682190809453, -0.0157944908576907, 8.81223860011747E-05, -2.17461651183501E-07, 1.96630278356455E-10];
			object.mksThermalConductivityVaporCoefficients('Ethyl acetate') = [108.264251112436, 0.501673917124385, 45681106.4588668, 2348697720.48655];
			object.mksVaporPressureLiquidCoefficients('Ethyl acetate') = [94.5606934026216, -7106.78973464377, 0, 0, -10.8907394652932, 8.65251697890424E-06, 2];
			object.mksViscosityLiquidCoefficients('Ethyl acetate') = [-78.5620420494662, 2907.32602298635, 11.1093718882292, -2.54020060222279E-05];
			object.mksViscosityVaporCoefficients('Ethyl acetate') = [4.52205183729903E-06, 0.274014797961392, 415.278101470084, 46597.8574222867];
			object.mksAcentricFactorValues('Ethyl acetate') = 0.362;
			object.mksBoilingPointValues('Ethyl acetate') = 350.3;
			object.mksCriticalCompressibilityValues('Ethyl acetate') = 0.252;
			object.mksCriticalPressureValues('Ethyl acetate') = 3830000;
			object.mksCriticalTemperatureValues('Ethyl acetate') = 523.2;
			object.mksCriticalVolumeValues('Ethyl acetate') = 0.286;
			object.mksDipoleMomentValues('Ethyl acetate') = 5.9374392E-30;
			object.mksEnthalpyCombustion298Values('Ethyl acetate') = -2237497040;
			object.mksEnthalpyFormationVapor298Values('Ethyl acetate') = -444100000;
			object.mksEnthalpyFusionTmValues('Ethyl acetate') = 10485000;
			object.mksEnthalpyVaporizationTbValues('Ethyl acetate') = 31902089.0949967;
			object.mksFlammabilityLimitLowerValues('Ethyl acetate') = 2;
			object.mksFlammabilityLimitUpperValues('Ethyl acetate') = 11.5;
			object.mksFlashPointClosedCupValues('Ethyl acetate') = 268.705555555556;
			object.mksGibbsEnergyFormationVapor298Values('Ethyl acetate') = -313160000;
			object.mksMeltingPointValues('Ethyl acetate') = 189.6;
			object.mksMolecularWeightValues('Ethyl acetate') = 88.1051;
			object.mksRadiusGyrationValues('Ethyl acetate') = 3.468E-10;
			object.mksSolubilityParameterTotalValues('Ethyl acetate') = 18200;
			object.mksRefractiveIndexLiquid293Values('Ethyl acetate') = 1.37233;
			object.mksAutoIgnitionTemperatureValues('Ethyl acetate') = 699.816666666667;
			if( nargin > 0 )
				names{end+1} = 'Ethyl acetate';
			end

			% n-Hexane
			object.mksDensityLiquidCoefficients('n-Hexane') = [1.32666526529024, 0.418942413156576, 17184.2275818043, -0.0070070357225577];
			object.mksDensitySolidCoefficients('n-Hexane') = [10.657, -0.004653];
			object.mksEnthalpyVaporizationCoefficients('n-Hexane') = [41792900.2886331, 0.2520219316275, 0.130485049443358];
			object.mksIsobaricHeatCapacityLiquidCoefficients('n-Hexane') = [-1019821.42870141, 18721.4016466913, -110.049396405129, 0.285549400876729, -0.000272246271491392];
			object.mksIsobaricHeatCapacityVaporCoefficients('n-Hexane') = [55348.9982273188, 246228.686696989, 723.019300695011, 92756.3672677929, 345.183174028017];
			object.mksSurfaceTensionLiquidCoefficients('n-Hexane') = [0.0480755149542094, 0.780256622275141, 0.56178541722006];
			object.mksThermalConductivityLiquidCoefficients('n-Hexane') = [0.756405462500389, -0.0094583661445604, 5.64038091359954E-05, -1.50380290035225E-07, 1.46314511749532E-10];
			object.mksThermalConductivityVaporCoefficients('n-Hexane') = [111.927435343892, 0.515399374202061, 40545180.7928067, 4348115592.81386];
			object.mksVaporPressureLiquidCoefficients('n-Hexane') = [-32.1922443513369, -2878.02571191109, 0, 0, 9.60387691558445, -3.33927248275069E-05, 2];
			object.mksViscosityLiquidCoefficients('n-Hexane') = [-6.26681998023202, 774.217629378707, -0.852686123973066, 4.42431965642668E-06];
			object.mksViscosityVaporCoefficients('n-Hexane') = [3.30077174080532E-06, 0.507609977494148, 4208.69761737952, -552294.152157624];
			object.mksAcentricFactorValues('n-Hexane') = 0.299;
			object.mksBoilingPointValues('n-Hexane') = 341.85;
			object.mksCriticalCompressibilityValues('n-Hexane') = 0.264;
			object.mksCriticalPressureValues('n-Hexane') = 3012000;
			object.mksCriticalTemperatureValues('n-Hexane') = 507.5;
			object.mksCriticalVolumeValues('n-Hexane') = 0.37;
			object.mksDipoleMomentValues('n-Hexane') = 0;
			object.mksEnthalpyCombustion298Values('n-Hexane') = -4163121840;
			object.mksEnthalpyFormationVapor298Values('n-Hexane') = -167280000;
			object.mksEnthalpyFusionTmValues('n-Hexane') = 11296000;
			object.mksEnthalpyVaporizationTbValues('n-Hexane') = 28870447.3729476;
			object.mksFlammabilityLimitLowerValues('n-Hexane') = 1.1;
			object.mksFlammabilityLimitUpperValues('n-Hexane') = 7.5;
			object.mksFlashPointClosedCupValues('n-Hexane') = 251.483333333333;
			object.mksGibbsEnergyFormationVapor298Values('n-Hexane') = 14050000;
			object.mksMeltingPointValues('n-Hexane') = 177.79;
			object.mksMolecularWeightValues('n-Hexane') = 86.177;
			object.mksRadiusGyrationValues('n-Hexane') = 3.769E-10;
			object.mksSolubilityParameterTotalValues('n-Hexane') = 14900;
			object.mksRefractiveIndexLiquid293Values('n-Hexane') = 1.3723;
			object.mksAutoIgnitionTemperatureValues('n-Hexane') = 498.15;
			if( nargin > 0 )
				names{end+1} = 'n-Hexane';
			end

			% Toluene
			object.mksDensityLiquidCoefficients('Toluene') = [1.50533202087661, 0.378125845395845, -2166.73872667352, -1.09996857639432];
			object.mksEnthalpyVaporizationCoefficients('Toluene') = [51288492.0339854, 0.46813601594588, -0.0930204957695851];
			object.mksIsobaricHeatCapacityLiquidCoefficients('Toluene') = [152561.042737948, -171.450263166134, -0.252245444021734, 0.004973743113058, -6.79934907793946E-06];
			object.mksIsobaricHeatCapacitySolidCoefficients('Toluene') = [23040.1891513388, 673.093410863589, -2.32633640891823, 0.0081843359260949, -1.09303477205316E-05];
			object.mksIsobaricHeatCapacityVaporCoefficients('Toluene') = [74251.7136439635, 197780.730354137, 1006.50773248138, 88529.8964377563, 614.592888157575];
			object.mksSurfaceTensionLiquidCoefficients('Toluene') = [0.0587061529471474, 0.837799936507821, 0.455481445299684];
			object.mksThermalConductivityLiquidCoefficients('Toluene') = [1.00023920699017, -0.0114270806906344, 5.85732063641616E-05, -1.3515692157411E-07, 1.15562025486388E-10];
			object.mksThermalConductivityVaporCoefficients('Toluene') = [107.855843460492, 0.51368652901904, 42500597.6912509, 7397166597.75434];
			object.mksVaporPressureLiquidCoefficients('Toluene') = [83.3495807606274, -6993.67956004541, 0, 0, -9.16333455341968, 6.26965481466175E-06, 2];
			object.mksViscosityLiquidCoefficients('Toluene') = [-10.4819312689531, 1020.62743194056, -0.0747154331745934, -7.01758693879626E-08];
			object.mksViscosityVaporCoefficients('Toluene') = [4.67282038753904E-06, 0.336894600696807, 1261.30081524765, -55570.873921681];
			object.mksAcentricFactorValues('Toluene') = 0.263;
			object.mksBoilingPointValues('Toluene') = 383.78;
			object.mksCriticalCompressibilityValues('Toluene') = 0.264;
			object.mksCriticalPressureValues('Toluene') = 4108000;
			object.mksCriticalTemperatureValues('Toluene') = 591.75;
			object.mksCriticalVolumeValues('Toluene') = 0.316;
			object.mksDipoleMomentValues('Toluene') = 1.2008304E-30;
			object.mksEnthalpyCombustion298Values('Toluene') = -3909900000;
			object.mksEnthalpyFormationVapor298Values('Toluene') = 50000000;
			object.mksEnthalpyFusionTmValues('Toluene') = 7927000;
			object.mksEnthalpyVaporizationTbValues('Toluene') = 33319036.4464389;
			object.mksFlammabilityLimitLowerValues('Toluene') = 1.1;
			object.mksFlammabilityLimitUpperValues('Toluene') = 7.1;
			object.mksFlashPointClosedCupValues('Toluene') = 280.7;
			object.mksGibbsEnergyFormationVapor298Values('Toluene') = 134880000;
			object.mksMeltingPointValues('Toluene') = 178.18;
			object.mksMolecularWeightValues('Toluene') = 92.141;
			object.mksRadiusGyrationValues('Toluene') = 3.472E-10;
			object.mksSolubilityParameterTotalValues('Toluene') = 18300;
			object.mksRefractiveIndexLiquid293Values('Toluene') = 1.49682;
			object.mksAutoIgnitionTemperatureValues('Toluene') = 753.15;
			if( nargin > 0 )
				names{end+1} = 'Toluene';
			end

			% Vinyl chloride
			object.mksDensityLiquidCoefficients('Vinyl chloride') = [1.87448794701961, 0.289494948646953, 354607.888095256, 469.160473070281];
			object.mksEnthalpyVaporizationCoefficients('Vinyl chloride') = [27475301.3318854, 0.247793007716049, 0.0831746086061254];
			object.mksIsobaricHeatCapacityLiquidCoefficients('Vinyl chloride') = [118207.065186521, -808.591640166033, 5.5417178836691, -0.0157631256495955, 1.80177407683916E-05];
			object.mksIsobaricHeatCapacitySolidCoefficients('Vinyl chloride') = [10990.3423830538, 396.487958025833, -2.65776074693354, 0.0144647876614416, -3.03035899081713E-05];
			object.mksIsobaricHeatCapacityVaporCoefficients('Vinyl chloride') = [39427.2092847134, -2.60214341322834E+17, -32948470517381.4, 63842.7196851099, 651.949348862645];
			object.mksSurfaceTensionLiquidCoefficients('Vinyl chloride') = [0.0604240433245908, 1.22222222222222, -5.98982363393694E-17];
			object.mksThermalConductivityLiquidCoefficients('Vinyl chloride') = [0.210363436351344, -0.000273376009722243, -2.25588613665282E-07, 4.13596066651952E-10, -1.16097464968064E-12];
			object.mksThermalConductivityVaporCoefficients('Vinyl chloride') = [109.601365816909, 0.49658083013276, 51442812.356046, 158939277.104989];
			object.mksVaporPressureLiquidCoefficients('Vinyl chloride') = [-308.823849308891, 3663.08035562981, 0, 0, 58.4954431532003, -0.000282456060584063, 2];
			object.mksViscosityLiquidCoefficients('Vinyl chloride') = [-20.3220376155081, 718.746441161128, 1.87433717733551, -1.71840937661899E-05];
			object.mksViscosityVaporCoefficients('Vinyl chloride') = [5.72490140719013E-06, 0.355685699119468, 1137.92091853748, -51971.8217434779];
			object.mksAcentricFactorValues('Vinyl chloride') = 0.133236859098415;
			object.mksBoilingPointValues('Vinyl chloride') = 259.78;
			object.mksCriticalCompressibilityValues('Vinyl chloride') = 0.269;
			object.mksCriticalPressureValues('Vinyl chloride') = 5300000;
			object.mksCriticalTemperatureValues('Vinyl chloride') = 429;
			object.mksCriticalVolumeValues('Vinyl chloride') = 0.181;
			object.mksDipoleMomentValues('Vinyl chloride') = 4.836678E-30;
			object.mksEnthalpyCombustion298Values('Vinyl chloride') = -1186331040;
			object.mksEnthalpyFormationVapor298Values('Vinyl chloride') = 21171040;
			object.mksEnthalpyFusionTmValues('Vinyl chloride') = 4916000;
			object.mksEnthalpyVaporizationTbValues('Vinyl chloride') = 21393255.470116;
			object.mksFlammabilityLimitLowerValues('Vinyl chloride') = 3.6;
			object.mksFlammabilityLimitUpperValues('Vinyl chloride') = 33;
			object.mksFlashPointClosedCupValues('Vinyl chloride') = 201.053012840267;
			object.mksGibbsEnergyFormationVapor298Values('Vinyl chloride') = 56280000;
			object.mksMeltingPointValues('Vinyl chloride') = 119.31;
			object.mksMolecularWeightValues('Vinyl chloride') = 62.499;
			object.mksRadiusGyrationValues('Vinyl chloride') = 2.049E-10;
			object.mksSolubilityParameterTotalValues('Vinyl chloride') = 15493.9084640749;
			object.mksAutoIgnitionTemperatureValues('Vinyl chloride') = 745.372222222222;
			if( nargin > 0 )
				names{end+1} = 'Vinyl chloride';
			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

