ThermoML Data file

	Right click here and Save Target to download the xml file
Information on ThermoML

<?xml version="1.0" encoding="UTF-8"?>  <DataReport xmlns:xsi="http://www.w3.org/2001/XMLSchema-instance" xsi:noNamespaceSchemaLocation="http://www.trc.nist.gov/ThermoML.xsd"> <Version> <nVersionMajor>2</nVersionMajor> <nVersionMinor>0</nVersionMinor> </Version> <Citation> <TRCRefID> <yrYrPub>2003</yrYrPub> <sAuthor1>tay</sAuthor1> <sAuthor2>tra</sAuthor2> <nAuthorn>0</nAuthorn> </TRCRefID> <eType>journal</eType> <eSourceType>Original</eSourceType> <sAuthor>Taylor, P. G.[Priscilla G.]</sAuthor> <sAuthor>Tran, A. M.[Anh M.]</sAuthor> <sAuthor>Charlton, A. K.[Amanda K.]</sAuthor> <sAuthor>Daniels, C.[Charlisa]</sAuthor> <sAuthor>Acree Jr., W. E.[William E.]</sAuthor> <sPubName>J. Chem. Eng. Data</sPubName> <yrPubYr>2003</yrPubYr> <dateCit>2003-11-17</dateCit> <sTitle>Solubility in Binary Solvent Mixtures: Anthracene Dissolved in Alcohol + Carbon Tetrachloride Mixtures at 298.2 K</sTitle> <sAbstract>Experimental solubilities are reported for anthracene dissolved in six binary alcohol + carbon tetrachloride solvent mixtures at 25 C. The alcohol cosolvents studied were 1-propanol, 2-propanol, 1-butanol, 2-butanol, 2-methyl-1-propanol, and 3-methyl-1-butanol. Results of these measurements are used to test a mathematical representation based upon the combined nearly ideal binary solvent (NIBS)/Redlich-Kister equation. For the six systems studied, the combined NIBS/Redlich-Kister equation was found to mathematically describe the experimental data to within an overall average absolute deviation of approximately 0.4%.</sAbstract> <sKeyword>anthracene solubilities</sKeyword> <sKeyword>carbon tetrachloride</sKeyword> <sKeyword>alcohol solvents</sKeyword> <sVol>48</sVol> <sPage>1603-1605</sPage> </Citation> <Compound> <RegNum> <nOrgNum>1</nOrgNum> </RegNum> <sCommonName>anthracene</sCommonName> <sFormulaMolec>C14H10</sFormulaMolec> <Sample> <nSampleNm>1</nSampleNm> <eSource>Commercial source</eSource> <purity> <nStep>1</nStep> <nPurityMol>99</nPurityMol> <nPurityMolDigits>2</nPurityMolDigits> <eAnalMeth>Not known</eAnalMeth> </purity> <purity> <nStep>2</nStep> <ePurifMethod>Crystallization from solution</ePurifMethod> </purity> <purity> <nStep>2</nStep> <nPurityMol>99</nPurityMol> <nPurityMolDigits>2</nPurityMolDigits> <eAnalMeth>Estimation</eAnalMeth> </purity> </Sample> </Compound> <Compound> <RegNum> <nOrgNum>2</nOrgNum> </RegNum> <sCommonName>carbon tetrachloride</sCommonName> <sFormulaMolec>CCl4</sFormulaMolec> <Sample> <nSampleNm>1</nSampleNm> <eSource>Commercial source</eSource> <purity> <nStep>1</nStep> <nPurityMol>99.5</nPurityMol> <nPurityMolDigits>3</nPurityMolDigits> <eAnalMeth>Not known</eAnalMeth> </purity> <purity> <nStep>2</nStep> <ePurifMethod>Fractional distillation</ePurifMethod> <ePurifMethod>Molecular sieve treatment</ePurifMethod> </purity> <purity> <nStep>2</nStep> <nPurityMol>99.7</nPurityMol> <nPurityMolDigits>3</nPurityMolDigits> <eAnalMeth>Gas chromatography</eAnalMeth> </purity> </Sample> </Compound> <Compound> <RegNum> <nOrgNum>3</nOrgNum> </RegNum> <sCommonName>1-propanol</sCommonName> <sFormulaMolec>C3H8O</sFormulaMolec> <Sample> <nSampleNm>1</nSampleNm> <eSource>Commercial source</eSource> <purity> <nStep>1</nStep> <nPurityMol>99</nPurityMol> <nPurityMolDigits>2</nPurityMolDigits> <eAnalMeth>Not known</eAnalMeth> </purity> <purity> <nStep>2</nStep> <ePurifMethod>Fractional distillation</ePurifMethod> <ePurifMethod>Molecular sieve treatment</ePurifMethod> </purity> <purity> <nStep>2</nStep> <nPurityMol>99.7</nPurityMol> <nPurityMolDigits>3</nPurityMolDigits> <eAnalMeth>Gas chromatography</eAnalMeth> </purity> </Sample> </Compound> <Compound> <RegNum> <nOrgNum>4</nOrgNum> </RegNum> <sCommonName>2-propanol</sCommonName> <sFormulaMolec>C3H8O</sFormulaMolec> <Sample> <nSampleNm>1</nSampleNm> <eSource>Commercial source</eSource> <purity> <nStep>1</nStep> <nPurityMol>99</nPurityMol> <nPurityMolDigits>2</nPurityMolDigits> <eAnalMeth>Not known</eAnalMeth> </purity> <purity> <nStep>2</nStep> <ePurifMethod>Fractional distillation</ePurifMethod> <ePurifMethod>Molecular sieve treatment</ePurifMethod> </purity> <purity> <nStep>2</nStep> <nPurityMol>99.7</nPurityMol> <nPurityMolDigits>3</nPurityMolDigits> <eAnalMeth>Gas chromatography</eAnalMeth> </purity> </Sample> </Compound> <Compound> <RegNum> <nOrgNum>5</nOrgNum> </RegNum> <sCommonName>1-butanol</sCommonName> <sFormulaMolec>C4H10O</sFormulaMolec> <Sample> <nSampleNm>1</nSampleNm> <eSource>Commercial source</eSource> <purity> <nStep>1</nStep> <nPurityMol>99</nPurityMol> <nPurityMolDigits>2</nPurityMolDigits> <eAnalMeth>Not known</eAnalMeth> </purity> <purity> <nStep>2</nStep> <ePurifMethod>Fractional distillation</ePurifMethod> <ePurifMethod>Molecular sieve treatment</ePurifMethod> </purity> <purity> <nStep>2</nStep> <nPurityMol>99.7</nPurityMol> <nPurityMolDigits>3</nPurityMolDigits> <eAnalMeth>Gas chromatography</eAnalMeth> </purity> </Sample> </Compound> <Compound> <RegNum> <nOrgNum>6</nOrgNum> </RegNum> <sCommonName>2-butanol, dl-</sCommonName> <sFormulaMolec>C4H10O</sFormulaMolec> <Sample> <nSampleNm>1</nSampleNm> <eSource>Commercial source</eSource> <purity> <nStep>1</nStep> <nPurityMol>99</nPurityMol> <nPurityMolDigits>2</nPurityMolDigits> <eAnalMeth>Not known</eAnalMeth> </purity> <purity> <nStep>2</nStep> <ePurifMethod>Fractional distillation</ePurifMethod> <ePurifMethod>Molecular sieve treatment</ePurifMethod> </purity> <purity> <nStep>2</nStep> <nPurityMol>99.7</nPurityMol> <nPurityMolDigits>3</nPurityMolDigits> <eAnalMeth>Gas chromatography</eAnalMeth> </purity> </Sample> </Compound> <Compound> <RegNum> <nOrgNum>7</nOrgNum> </RegNum> <sCommonName>2-methyl-1-propanol</sCommonName> <sFormulaMolec>C4H10O</sFormulaMolec> <Sample> <nSampleNm>1</nSampleNm> <eSource>Commercial source</eSource> <purity> <nStep>1</nStep> <nPurityMol>99.5</nPurityMol> <nPurityMolDigits>3</nPurityMolDigits> <eAnalMeth>Not known</eAnalMeth> </purity> <purity> <nStep>2</nStep> <ePurifMethod>Fractional distillation</ePurifMethod> <ePurifMethod>Molecular sieve treatment</ePurifMethod> </purity> <purity> <nStep>2</nStep> <nPurityMol>99.7</nPurityMol> <nPurityMolDigits>3</nPurityMolDigits> <eAnalMeth>Gas chromatography</eAnalMeth> </purity> </Sample> </Compound> <Compound> <RegNum> <nOrgNum>8</nOrgNum> </RegNum> <sCommonName>3-methyl-1-butanol</sCommonName> <sFormulaMolec>C5H12O</sFormulaMolec> <Sample> <nSampleNm>1</nSampleNm> <eSource>Commercial source</eSource> <purity> <nStep>1</nStep> <nPurityMol>99</nPurityMol> <nPurityMolDigits>2</nPurityMolDigits> <eAnalMeth>Not known</eAnalMeth> </purity> <purity> <nStep>2</nStep> <ePurifMethod>Fractional distillation</ePurifMethod> <ePurifMethod>Molecular sieve treatment</ePurifMethod> </purity> <purity> <nStep>2</nStep> <nPurityMol>99.7</nPurityMol> <nPurityMolDigits>3</nPurityMolDigits> <eAnalMeth>Gas chromatography</eAnalMeth> </purity> </Sample> </Compound> <PureOrMixtureData> <Component> <RegNum> <nOrgNum>2</nOrgNum> </RegNum> <nSampleNm>1</nSampleNm> </Component> <Component> <RegNum> <nOrgNum>3</nOrgNum> </RegNum> <nSampleNm>1</nSampleNm> </Component> <Component> <RegNum> <nOrgNum>1</nOrgNum> </RegNum> <nSampleNm>1</nSampleNm> </Component> <eExpPurpose>Principal objective of the work</eExpPurpose> <sCompiler>JCE</sCompiler> <sContributor>JCE</sContributor> <dateDateAdded>8/5/2003</dateDateAdded> <Property> <nPropNumber>1</nPropNumber> <Property-MethodID> <PropertyGroup> <CompositionAtPhaseEquilibrium> <ePropName>Mole fraction</ePropName> <eMethodName>Other</eMethodName> </CompositionAtPhaseEquilibrium> </PropertyGroup> <RegNum> <nOrgNum>1</nOrgNum> </RegNum> </Property-MethodID> <PropPhaseID> <ePropPhase>Liquid</ePropPhase> </PropPhaseID> <ePresentation>Direct value, X</ePresentation> </Property> <PhaseID> <ePhase>Liquid</ePhase> </PhaseID> <PhaseID> <ePhase>Crystal</ePhase> </PhaseID> <Constraint> <ConstraintID> <ConstraintType> <ePressure>Pressure, kPa</ePressure> </ConstraintType> </ConstraintID> <nConstraintValue>101</nConstraintValue> <nConstrDigits>3</nConstrDigits> </Constraint> <Constraint> <ConstraintID> <ConstraintType> <eTemperature>Temperature, K</eTemperature> </ConstraintType> </ConstraintID> <nConstraintValue>298</nConstraintValue> <nConstrDigits>3</nConstrDigits> </Constraint> <Variable> <nVarNumber>1</nVarNumber> <VariableID> <VariableType> <eSolventComposition>Solvent: Mole fraction</eSolventComposition> </VariableType> <RegNum> <nOrgNum>2</nOrgNum> </RegNum> </VariableID> <VarPhaseID> <eVarPhase>Liquid</eVarPhase> </VarPhaseID> <Solvent> <RegNum> <nOrgNum>2</nOrgNum> </RegNum> <RegNum> <nOrgNum>3</nOrgNum> </RegNum> </Solvent> </Variable> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>0</nVarValue> <nVarDigits>0</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>.000591</nPropValue> <nPropDigits>3</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.0962</nVarValue> <nVarDigits>3</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>.00077</nPropValue> <nPropDigits>3</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.1768</nVarValue> <nVarDigits>4</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>.000965</nPropValue> <nPropDigits>3</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.3363</nVarValue> <nVarDigits>4</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>.001499</nPropValue> <nPropDigits>4</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.4363</nVarValue> <nVarDigits>4</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>.001975</nPropValue> <nPropDigits>4</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.5579</nVarValue> <nVarDigits>4</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>.002651</nPropValue> <nPropDigits>4</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.765</nVarValue> <nVarDigits>4</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>.003756</nPropValue> <nPropDigits>4</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.8485</nVarValue> <nVarDigits>4</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>.004163</nPropValue> <nPropDigits>4</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>1</nVarValue> <nVarDigits>5</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>.004622</nPropValue> <nPropDigits>4</nPropDigits> </PropertyValue> </NumValues> </PureOrMixtureData> <PureOrMixtureData> <Component> <RegNum> <nOrgNum>2</nOrgNum> </RegNum> <nSampleNm>1</nSampleNm> </Component> <Component> <RegNum> <nOrgNum>4</nOrgNum> </RegNum> <nSampleNm>1</nSampleNm> </Component> <Component> <RegNum> <nOrgNum>1</nOrgNum> </RegNum> <nSampleNm>1</nSampleNm> </Component> <eExpPurpose>Principal objective of the work</eExpPurpose> <sCompiler>JCE</sCompiler> <sContributor>JCE</sContributor> <dateDateAdded>8/5/2003</dateDateAdded> <Property> <nPropNumber>1</nPropNumber> <Property-MethodID> <PropertyGroup> <CompositionAtPhaseEquilibrium> <ePropName>Mole fraction</ePropName> <eMethodName>Other</eMethodName> </CompositionAtPhaseEquilibrium> </PropertyGroup> <RegNum> <nOrgNum>1</nOrgNum> </RegNum> </Property-MethodID> <PropPhaseID> <ePropPhase>Liquid</ePropPhase> </PropPhaseID> <ePresentation>Direct value, X</ePresentation> </Property> <PhaseID> <ePhase>Liquid</ePhase> </PhaseID> <PhaseID> <ePhase>Crystal</ePhase> </PhaseID> <Constraint> <ConstraintID> <ConstraintType> <ePressure>Pressure, kPa</ePressure> </ConstraintType> </ConstraintID> <nConstraintValue>101</nConstraintValue> <nConstrDigits>3</nConstrDigits> </Constraint> <Constraint> <ConstraintID> <ConstraintType> <eTemperature>Temperature, K</eTemperature> </ConstraintType> </ConstraintID> <nConstraintValue>298</nConstraintValue> <nConstrDigits>3</nConstrDigits> </Constraint> <Variable> <nVarNumber>1</nVarNumber> <VariableID> <VariableType> <eSolventComposition>Solvent: Mole fraction</eSolventComposition> </VariableType> <RegNum> <nOrgNum>2</nOrgNum> </RegNum> </VariableID> <VarPhaseID> <eVarPhase>Liquid</eVarPhase> </VarPhaseID> <Solvent> <RegNum> <nOrgNum>2</nOrgNum> </RegNum> <RegNum> <nOrgNum>4</nOrgNum> </RegNum> </Solvent> </Variable> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>0</nVarValue> <nVarDigits>0</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>.000411</nPropValue> <nPropDigits>3</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.0947</nVarValue> <nVarDigits>3</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>.000581</nPropValue> <nPropDigits>3</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.1836</nVarValue> <nVarDigits>4</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>.000809</nPropValue> <nPropDigits>3</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.3447</nVarValue> <nVarDigits>4</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>.001406</nPropValue> <nPropDigits>4</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.434</nVarValue> <nVarDigits>4</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>.001871</nPropValue> <nPropDigits>4</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.5843</nVarValue> <nVarDigits>4</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>.002703</nPropValue> <nPropDigits>4</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.7524</nVarValue> <nVarDigits>4</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>.003696</nPropValue> <nPropDigits>4</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.8736</nVarValue> <nVarDigits>4</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>.004284</nPropValue> <nPropDigits>4</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>1</nVarValue> <nVarDigits>5</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>.004622</nPropValue> <nPropDigits>4</nPropDigits> </PropertyValue> </NumValues> </PureOrMixtureData> <PureOrMixtureData> <Component> <RegNum> <nOrgNum>2</nOrgNum> </RegNum> <nSampleNm>1</nSampleNm> </Component> <Component> <RegNum> <nOrgNum>5</nOrgNum> </RegNum> <nSampleNm>1</nSampleNm> </Component> <Component> <RegNum> <nOrgNum>1</nOrgNum> </RegNum> <nSampleNm>1</nSampleNm> </Component> <eExpPurpose>Principal objective of the work</eExpPurpose> <sCompiler>JCE</sCompiler> <sContributor>JCE</sContributor> <dateDateAdded>8/5/2003</dateDateAdded> <Property> <nPropNumber>1</nPropNumber> <Property-MethodID> <PropertyGroup> <CompositionAtPhaseEquilibrium> <ePropName>Mole fraction</ePropName> <eMethodName>Other</eMethodName> </CompositionAtPhaseEquilibrium> </PropertyGroup> <RegNum> <nOrgNum>1</nOrgNum> </RegNum> </Property-MethodID> <PropPhaseID> <ePropPhase>Liquid</ePropPhase> </PropPhaseID> <ePresentation>Direct value, X</ePresentation> </Property> <PhaseID> <ePhase>Liquid</ePhase> </PhaseID> <PhaseID> <ePhase>Crystal</ePhase> </PhaseID> <Constraint> <ConstraintID> <ConstraintType> <ePressure>Pressure, kPa</ePressure> </ConstraintType> </ConstraintID> <nConstraintValue>101</nConstraintValue> <nConstrDigits>3</nConstrDigits> </Constraint> <Constraint> <ConstraintID> <ConstraintType> <eTemperature>Temperature, K</eTemperature> </ConstraintType> </ConstraintID> <nConstraintValue>298</nConstraintValue> <nConstrDigits>3</nConstrDigits> </Constraint> <Variable> <nVarNumber>1</nVarNumber> <VariableID> <VariableType> <eSolventComposition>Solvent: Mole fraction</eSolventComposition> </VariableType> <RegNum> <nOrgNum>2</nOrgNum> </RegNum> </VariableID> <VarPhaseID> <eVarPhase>Liquid</eVarPhase> </VarPhaseID> <Solvent> <RegNum> <nOrgNum>2</nOrgNum> </RegNum> <RegNum> <nOrgNum>5</nOrgNum> </RegNum> </Solvent> </Variable> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>0</nVarValue> <nVarDigits>0</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>.000801</nPropValue> <nPropDigits>3</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.0983</nVarValue> <nVarDigits>3</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>.000953</nPropValue> <nPropDigits>3</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.195</nVarValue> <nVarDigits>4</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>.001178</nPropValue> <nPropDigits>4</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.3955</nVarValue> <nVarDigits>4</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>.001833</nPropValue> <nPropDigits>4</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.4886</nVarValue> <nVarDigits>4</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>.002236</nPropValue> <nPropDigits>4</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.5864</nVarValue> <nVarDigits>4</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>.002768</nPropValue> <nPropDigits>4</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.7894</nVarValue> <nVarDigits>4</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>.003844</nPropValue> <nPropDigits>4</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.8969</nVarValue> <nVarDigits>4</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>.004364</nPropValue> <nPropDigits>4</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>1</nVarValue> <nVarDigits>5</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>.004622</nPropValue> <nPropDigits>4</nPropDigits> </PropertyValue> </NumValues> </PureOrMixtureData> <PureOrMixtureData> <Component> <RegNum> <nOrgNum>2</nOrgNum> </RegNum> <nSampleNm>1</nSampleNm> </Component> <Component> <RegNum> <nOrgNum>6</nOrgNum> </RegNum> <nSampleNm>1</nSampleNm> </Component> <Component> <RegNum> <nOrgNum>1</nOrgNum> </RegNum> <nSampleNm>1</nSampleNm> </Component> <eExpPurpose>Principal objective of the work</eExpPurpose> <sCompiler>JCE</sCompiler> <sContributor>JCE</sContributor> <dateDateAdded>8/5/2003</dateDateAdded> <Property> <nPropNumber>1</nPropNumber> <Property-MethodID> <PropertyGroup> <CompositionAtPhaseEquilibrium> <ePropName>Mole fraction</ePropName> <eMethodName>Other</eMethodName> </CompositionAtPhaseEquilibrium> </PropertyGroup> <RegNum> <nOrgNum>1</nOrgNum> </RegNum> </Property-MethodID> <PropPhaseID> <ePropPhase>Liquid</ePropPhase> </PropPhaseID> <ePresentation>Direct value, X</ePresentation> </Property> <PhaseID> <ePhase>Liquid</ePhase> </PhaseID> <PhaseID> <ePhase>Crystal</ePhase> </PhaseID> <Constraint> <ConstraintID> <ConstraintType> <ePressure>Pressure, kPa</ePressure> </ConstraintType> </ConstraintID> <nConstraintValue>101</nConstraintValue> <nConstrDigits>3</nConstrDigits> </Constraint> <Constraint> <ConstraintID> <ConstraintType> <eTemperature>Temperature, K</eTemperature> </ConstraintType> </ConstraintID> <nConstraintValue>298</nConstraintValue> <nConstrDigits>3</nConstrDigits> </Constraint> <Variable> <nVarNumber>1</nVarNumber> <VariableID> <VariableType> <eSolventComposition>Solvent: Mole fraction</eSolventComposition> </VariableType> <RegNum> <nOrgNum>2</nOrgNum> </RegNum> </VariableID> <VarPhaseID> <eVarPhase>Liquid</eVarPhase> </VarPhaseID> <Solvent> <RegNum> <nOrgNum>2</nOrgNum> </RegNum> <RegNum> <nOrgNum>6</nOrgNum> </RegNum> </Solvent> </Variable> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>0</nVarValue> <nVarDigits>0</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>.000585</nPropValue> <nPropDigits>3</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.1231</nVarValue> <nVarDigits>4</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>.000863</nPropValue> <nPropDigits>3</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.207</nVarValue> <nVarDigits>4</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>.001109</nPropValue> <nPropDigits>4</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.3943</nVarValue> <nVarDigits>4</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>.001815</nPropValue> <nPropDigits>4</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.4872</nVarValue> <nVarDigits>4</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>.002252</nPropValue> <nPropDigits>4</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.5925</nVarValue> <nVarDigits>4</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>.002802</nPropValue> <nPropDigits>4</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.7912</nVarValue> <nVarDigits>4</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>.003882</nPropValue> <nPropDigits>4</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.8834</nVarValue> <nVarDigits>4</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>.004306</nPropValue> <nPropDigits>4</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>1</nVarValue> <nVarDigits>5</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>.004622</nPropValue> <nPropDigits>4</nPropDigits> </PropertyValue> </NumValues> </PureOrMixtureData> <PureOrMixtureData> <Component> <RegNum> <nOrgNum>2</nOrgNum> </RegNum> <nSampleNm>1</nSampleNm> </Component> <Component> <RegNum> <nOrgNum>7</nOrgNum> </RegNum> <nSampleNm>1</nSampleNm> </Component> <Component> <RegNum> <nOrgNum>1</nOrgNum> </RegNum> <nSampleNm>1</nSampleNm> </Component> <eExpPurpose>Principal objective of the work</eExpPurpose> <sCompiler>JCE</sCompiler> <sContributor>JCE</sContributor> <dateDateAdded>8/5/2003</dateDateAdded> <Property> <nPropNumber>1</nPropNumber> <Property-MethodID> <PropertyGroup> <CompositionAtPhaseEquilibrium> <ePropName>Mole fraction</ePropName> <eMethodName>Other</eMethodName> </CompositionAtPhaseEquilibrium> </PropertyGroup> <RegNum> <nOrgNum>1</nOrgNum> </RegNum> </Property-MethodID> <PropPhaseID> <ePropPhase>Liquid</ePropPhase> </PropPhaseID> <ePresentation>Direct value, X</ePresentation> </Property> <PhaseID> <ePhase>Liquid</ePhase> </PhaseID> <PhaseID> <ePhase>Crystal</ePhase> </PhaseID> <Constraint> <ConstraintID> <ConstraintType> <ePressure>Pressure, kPa</ePressure> </ConstraintType> </ConstraintID> <nConstraintValue>101</nConstraintValue> <nConstrDigits>3</nConstrDigits> </Constraint> <Constraint> <ConstraintID> <ConstraintType> <eTemperature>Temperature, K</eTemperature> </ConstraintType> </ConstraintID> <nConstraintValue>298</nConstraintValue> <nConstrDigits>3</nConstrDigits> </Constraint> <Variable> <nVarNumber>1</nVarNumber> <VariableID> <VariableType> <eSolventComposition>Solvent: Mole fraction</eSolventComposition> </VariableType> <RegNum> <nOrgNum>2</nOrgNum> </RegNum> </VariableID> <VarPhaseID> <eVarPhase>Liquid</eVarPhase> </VarPhaseID> <Solvent> <RegNum> <nOrgNum>2</nOrgNum> </RegNum> <RegNum> <nOrgNum>7</nOrgNum> </RegNum> </Solvent> </Variable> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>0</nVarValue> <nVarDigits>0</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>.00047</nPropValue> <nPropDigits>3</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.1281</nVarValue> <nVarDigits>4</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>.000696</nPropValue> <nPropDigits>3</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.2088</nVarValue> <nVarDigits>4</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>.000897</nPropValue> <nPropDigits>3</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.3831</nVarValue> <nVarDigits>4</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>.001489</nPropValue> <nPropDigits>4</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.495</nVarValue> <nVarDigits>4</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>.002049</nPropValue> <nPropDigits>4</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.6027</nVarValue> <nVarDigits>4</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>.002627</nPropValue> <nPropDigits>4</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.7893</nVarValue> <nVarDigits>4</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>.003718</nPropValue> <nPropDigits>4</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.8936</nVarValue> <nVarDigits>4</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>.004283</nPropValue> <nPropDigits>4</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>1</nVarValue> <nVarDigits>5</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>.004622</nPropValue> <nPropDigits>4</nPropDigits> </PropertyValue> </NumValues> </PureOrMixtureData> <PureOrMixtureData> <Component> <RegNum> <nOrgNum>2</nOrgNum> </RegNum> <nSampleNm>1</nSampleNm> </Component> <Component> <RegNum> <nOrgNum>1</nOrgNum> </RegNum> <nSampleNm>1</nSampleNm> </Component> <Component> <RegNum> <nOrgNum>8</nOrgNum> </RegNum> <nSampleNm>1</nSampleNm> </Component> <eExpPurpose>Principal objective of the work</eExpPurpose> <sCompiler>JCE</sCompiler> <sContributor>JCE</sContributor> <dateDateAdded>8/5/2003</dateDateAdded> <Property> <nPropNumber>1</nPropNumber> <Property-MethodID> <PropertyGroup> <CompositionAtPhaseEquilibrium> <ePropName>Mole fraction</ePropName> <eMethodName>Other</eMethodName> </CompositionAtPhaseEquilibrium> </PropertyGroup> <RegNum> <nOrgNum>1</nOrgNum> </RegNum> </Property-MethodID> <PropPhaseID> <ePropPhase>Liquid</ePropPhase> </PropPhaseID> <ePresentation>Direct value, X</ePresentation> </Property> <PhaseID> <ePhase>Liquid</ePhase> </PhaseID> <PhaseID> <ePhase>Crystal</ePhase> </PhaseID> <Constraint> <ConstraintID> <ConstraintType> <eTemperature>Temperature, K</eTemperature> </ConstraintType> </ConstraintID> <nConstraintValue>298</nConstraintValue> <nConstrDigits>3</nConstrDigits> </Constraint> <Constraint> <ConstraintID> <ConstraintType> <ePressure>Pressure, kPa</ePressure> </ConstraintType> </ConstraintID> <nConstraintValue>101</nConstraintValue> <nConstrDigits>3</nConstrDigits> </Constraint> <Variable> <nVarNumber>1</nVarNumber> <VariableID> <VariableType> <eSolventComposition>Solvent: Mole fraction</eSolventComposition> </VariableType> <RegNum> <nOrgNum>2</nOrgNum> </RegNum> </VariableID> <VarPhaseID> <eVarPhase>Liquid</eVarPhase> </VarPhaseID> <Solvent> <RegNum> <nOrgNum>2</nOrgNum> </RegNum> <RegNum> <nOrgNum>8</nOrgNum> </RegNum> </Solvent> </Variable> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>0</nVarValue> <nVarDigits>0</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>.000727</nPropValue> <nPropDigits>3</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.1181</nVarValue> <nVarDigits>4</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>.000926</nPropValue> <nPropDigits>3</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.2261</nVarValue> <nVarDigits>4</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>.001187</nPropValue> <nPropDigits>4</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.4333</nVarValue> <nVarDigits>4</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>.001927</nPropValue> <nPropDigits>4</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.5339</nVarValue> <nVarDigits>4</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>.00239</nPropValue> <nPropDigits>4</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.6336</nVarValue> <nVarDigits>4</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>.002922</nPropValue> <nPropDigits>4</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.8162</nVarValue> <nVarDigits>4</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>.003864</nPropValue> <nPropDigits>4</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.9003</nVarValue> <nVarDigits>4</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>.004312</nPropValue> <nPropDigits>4</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>1</nVarValue> <nVarDigits>5</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>.004622</nPropValue> <nPropDigits>4</nPropDigits> </PropertyValue> </NumValues> </PureOrMixtureData> <PureOrMixtureData> <Component> <RegNum> <nOrgNum>3</nOrgNum> </RegNum> <nSampleNm>1</nSampleNm> </Component> <Component> <RegNum> <nOrgNum>1</nOrgNum> </RegNum> <nSampleNm>1</nSampleNm> </Component> <eExpPurpose>Principal objective of the work</eExpPurpose> <sCompiler>RDC</sCompiler> <sContributor>TRC</sContributor> <dateDateAdded>11/14/2003</dateDateAdded> <Property> <nPropNumber>1</nPropNumber> <Property-MethodID> <PropertyGroup> <CompositionAtPhaseEquilibrium> <ePropName>Mole fraction</ePropName> <eMethodName>Other</eMethodName> </CompositionAtPhaseEquilibrium> </PropertyGroup> <RegNum> <nOrgNum>1</nOrgNum> </RegNum> </Property-MethodID> <PropPhaseID> <ePropPhase>Liquid</ePropPhase> </PropPhaseID> <ePresentation>Direct value, X</ePresentation> </Property> <PhaseID> <ePhase>Liquid</ePhase> </PhaseID> <PhaseID> <ePhase>Crystal</ePhase> </PhaseID> <Variable> <nVarNumber>1</nVarNumber> <VariableID> <VariableType> <eTemperature>Temperature, K</eTemperature> </VariableType> </VariableID> </Variable> <Variable> <nVarNumber>2</nVarNumber> <VariableID> <VariableType> <ePressure>Pressure, kPa</ePressure> </VariableType> </VariableID> </Variable> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>298</nVarValue> <nVarDigits>3</nVarDigits> </VariableValue> <VariableValue> <nVarNumber>2</nVarNumber> <nVarValue>101</nVarValue> <nVarDigits>3</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>.000591</nPropValue> <nPropDigits>3</nPropDigits> </PropertyValue> </NumValues> </PureOrMixtureData> <PureOrMixtureData> <Component> <RegNum> <nOrgNum>2</nOrgNum> </RegNum> <nSampleNm>1</nSampleNm> </Component> <Component> <RegNum> <nOrgNum>1</nOrgNum> </RegNum> <nSampleNm>1</nSampleNm> </Component> <eExpPurpose>Principal objective of the work</eExpPurpose> <sCompiler>RDC</sCompiler> <sContributor>TRC</sContributor> <dateDateAdded>11/14/2003</dateDateAdded> <Property> <nPropNumber>1</nPropNumber> <Property-MethodID> <PropertyGroup> <CompositionAtPhaseEquilibrium> <ePropName>Mole fraction</ePropName> <eMethodName>Other</eMethodName> </CompositionAtPhaseEquilibrium> </PropertyGroup> <RegNum> <nOrgNum>1</nOrgNum> </RegNum> </Property-MethodID> <PropPhaseID> <ePropPhase>Liquid</ePropPhase> </PropPhaseID> <ePresentation>Direct value, X</ePresentation> </Property> <PhaseID> <ePhase>Liquid</ePhase> </PhaseID> <PhaseID> <ePhase>Crystal</ePhase> </PhaseID> <Variable> <nVarNumber>1</nVarNumber> <VariableID> <VariableType> <eTemperature>Temperature, K</eTemperature> </VariableType> </VariableID> </Variable> <Variable> <nVarNumber>2</nVarNumber> <VariableID> <VariableType> <ePressure>Pressure, kPa</ePressure> </VariableType> </VariableID> </Variable> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>298</nVarValue> <nVarDigits>3</nVarDigits> </VariableValue> <VariableValue> <nVarNumber>2</nVarNumber> <nVarValue>101</nVarValue> <nVarDigits>3</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>.004622</nPropValue> <nPropDigits>4</nPropDigits> </PropertyValue> </NumValues> </PureOrMixtureData> <PureOrMixtureData> <Component> <RegNum> <nOrgNum>4</nOrgNum> </RegNum> <nSampleNm>1</nSampleNm> </Component> <Component> <RegNum> <nOrgNum>1</nOrgNum> </RegNum> <nSampleNm>1</nSampleNm> </Component> <eExpPurpose>Principal objective of the work</eExpPurpose> <sCompiler>RDC</sCompiler> <sContributor>TRC</sContributor> <dateDateAdded>11/14/2003</dateDateAdded> <Property> <nPropNumber>1</nPropNumber> <Property-MethodID> <PropertyGroup> <CompositionAtPhaseEquilibrium> <ePropName>Mole fraction</ePropName> <eMethodName>Other</eMethodName> </CompositionAtPhaseEquilibrium> </PropertyGroup> <RegNum> <nOrgNum>1</nOrgNum> </RegNum> </Property-MethodID> <PropPhaseID> <ePropPhase>Liquid</ePropPhase> </PropPhaseID> <ePresentation>Direct value, X</ePresentation> </Property> <PhaseID> <ePhase>Liquid</ePhase> </PhaseID> <PhaseID> <ePhase>Crystal</ePhase> </PhaseID> <Variable> <nVarNumber>1</nVarNumber> <VariableID> <VariableType> <eTemperature>Temperature, K</eTemperature> </VariableType> </VariableID> </Variable> <Variable> <nVarNumber>2</nVarNumber> <VariableID> <VariableType> <ePressure>Pressure, kPa</ePressure> </VariableType> </VariableID> </Variable> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>298</nVarValue> <nVarDigits>3</nVarDigits> </VariableValue> <VariableValue> <nVarNumber>2</nVarNumber> <nVarValue>101</nVarValue> <nVarDigits>3</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>.000411</nPropValue> <nPropDigits>3</nPropDigits> </PropertyValue> </NumValues> </PureOrMixtureData> <PureOrMixtureData> <Component> <RegNum> <nOrgNum>5</nOrgNum> </RegNum> <nSampleNm>1</nSampleNm> </Component> <Component> <RegNum> <nOrgNum>1</nOrgNum> </RegNum> <nSampleNm>1</nSampleNm> </Component> <eExpPurpose>Principal objective of the work</eExpPurpose> <sCompiler>RDC</sCompiler> <sContributor>TRC</sContributor> <dateDateAdded>11/14/2003</dateDateAdded> <Property> <nPropNumber>1</nPropNumber> <Property-MethodID> <PropertyGroup> <CompositionAtPhaseEquilibrium> <ePropName>Mole fraction</ePropName> <eMethodName>Other</eMethodName> </CompositionAtPhaseEquilibrium> </PropertyGroup> <RegNum> <nOrgNum>1</nOrgNum> </RegNum> </Property-MethodID> <PropPhaseID> <ePropPhase>Liquid</ePropPhase> </PropPhaseID> <ePresentation>Direct value, X</ePresentation> </Property> <PhaseID> <ePhase>Liquid</ePhase> </PhaseID> <PhaseID> <ePhase>Crystal</ePhase> </PhaseID> <Variable> <nVarNumber>1</nVarNumber> <VariableID> <VariableType> <eTemperature>Temperature, K</eTemperature> </VariableType> </VariableID> </Variable> <Variable> <nVarNumber>2</nVarNumber> <VariableID> <VariableType> <ePressure>Pressure, kPa</ePressure> </VariableType> </VariableID> </Variable> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>298</nVarValue> <nVarDigits>3</nVarDigits> </VariableValue> <VariableValue> <nVarNumber>2</nVarNumber> <nVarValue>101</nVarValue> <nVarDigits>3</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>.000801</nPropValue> <nPropDigits>3</nPropDigits> </PropertyValue> </NumValues> </PureOrMixtureData> <PureOrMixtureData> <Component> <RegNum> <nOrgNum>6</nOrgNum> </RegNum> <nSampleNm>1</nSampleNm> </Component> <Component> <RegNum> <nOrgNum>1</nOrgNum> </RegNum> <nSampleNm>1</nSampleNm> </Component> <eExpPurpose>Principal objective of the work</eExpPurpose> <sCompiler>RDC</sCompiler> <sContributor>TRC</sContributor> <dateDateAdded>11/14/2003</dateDateAdded> <Property> <nPropNumber>1</nPropNumber> <Property-MethodID> <PropertyGroup> <CompositionAtPhaseEquilibrium> <ePropName>Mole fraction</ePropName> <eMethodName>Other</eMethodName> </CompositionAtPhaseEquilibrium> </PropertyGroup> <RegNum> <nOrgNum>1</nOrgNum> </RegNum> </Property-MethodID> <PropPhaseID> <ePropPhase>Liquid</ePropPhase> </PropPhaseID> <ePresentation>Direct value, X</ePresentation> </Property> <PhaseID> <ePhase>Liquid</ePhase> </PhaseID> <PhaseID> <ePhase>Crystal</ePhase> </PhaseID> <Variable> <nVarNumber>1</nVarNumber> <VariableID> <VariableType> <eTemperature>Temperature, K</eTemperature> </VariableType> </VariableID> </Variable> <Variable> <nVarNumber>2</nVarNumber> <VariableID> <VariableType> <ePressure>Pressure, kPa</ePressure> </VariableType> </VariableID> </Variable> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>298</nVarValue> <nVarDigits>3</nVarDigits> </VariableValue> <VariableValue> <nVarNumber>2</nVarNumber> <nVarValue>101</nVarValue> <nVarDigits>3</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>.000585</nPropValue> <nPropDigits>3</nPropDigits> </PropertyValue> </NumValues> </PureOrMixtureData> <PureOrMixtureData> <Component> <RegNum> <nOrgNum>7</nOrgNum> </RegNum> <nSampleNm>1</nSampleNm> </Component> <Component> <RegNum> <nOrgNum>1</nOrgNum> </RegNum> <nSampleNm>1</nSampleNm> </Component> <eExpPurpose>Principal objective of the work</eExpPurpose> <sCompiler>RDC</sCompiler> <sContributor>TRC</sContributor> <dateDateAdded>11/14/2003</dateDateAdded> <Property> <nPropNumber>1</nPropNumber> <Property-MethodID> <PropertyGroup> <CompositionAtPhaseEquilibrium> <ePropName>Mole fraction</ePropName> <eMethodName>Other</eMethodName> </CompositionAtPhaseEquilibrium> </PropertyGroup> <RegNum> <nOrgNum>1</nOrgNum> </RegNum> </Property-MethodID> <PropPhaseID> <ePropPhase>Liquid</ePropPhase> </PropPhaseID> <ePresentation>Direct value, X</ePresentation> </Property> <PhaseID> <ePhase>Liquid</ePhase> </PhaseID> <PhaseID> <ePhase>Crystal</ePhase> </PhaseID> <Variable> <nVarNumber>1</nVarNumber> <VariableID> <VariableType> <eTemperature>Temperature, K</eTemperature> </VariableType> </VariableID> </Variable> <Variable> <nVarNumber>2</nVarNumber> <VariableID> <VariableType> <ePressure>Pressure, kPa</ePressure> </VariableType> </VariableID> </Variable> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>298</nVarValue> <nVarDigits>3</nVarDigits> </VariableValue> <VariableValue> <nVarNumber>2</nVarNumber> <nVarValue>101</nVarValue> <nVarDigits>3</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>.00047</nPropValue> <nPropDigits>3</nPropDigits> </PropertyValue> </NumValues> </PureOrMixtureData> <PureOrMixtureData> <Component> <RegNum> <nOrgNum>1</nOrgNum> </RegNum> <nSampleNm>1</nSampleNm> </Component> <Component> <RegNum> <nOrgNum>8</nOrgNum> </RegNum> <nSampleNm>1</nSampleNm> </Component> <eExpPurpose>Principal objective of the work</eExpPurpose> <sCompiler>RDC</sCompiler> <sContributor>TRC</sContributor> <dateDateAdded>11/14/2003</dateDateAdded> <Property> <nPropNumber>1</nPropNumber> <Property-MethodID> <PropertyGroup> <CompositionAtPhaseEquilibrium> <ePropName>Mole fraction</ePropName> <eMethodName>Other</eMethodName> </CompositionAtPhaseEquilibrium> </PropertyGroup> <RegNum> <nOrgNum>1</nOrgNum> </RegNum> </Property-MethodID> <PropPhaseID> <ePropPhase>Liquid</ePropPhase> </PropPhaseID> <ePresentation>Direct value, X</ePresentation> </Property> <PhaseID> <ePhase>Liquid</ePhase> </PhaseID> <PhaseID> <ePhase>Crystal</ePhase> </PhaseID> <Variable> <nVarNumber>1</nVarNumber> <VariableID> <VariableType> <ePressure>Pressure, kPa</ePressure> </VariableType> </VariableID> </Variable> <Variable> <nVarNumber>2</nVarNumber> <VariableID> <VariableType> <eTemperature>Temperature, K</eTemperature> </VariableType> </VariableID> </Variable> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>101</nVarValue> <nVarDigits>3</nVarDigits> </VariableValue> <VariableValue> <nVarNumber>2</nVarNumber> <nVarValue>298</nVarValue> <nVarDigits>3</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>.000727</nPropValue> <nPropDigits>3</nPropDigits> </PropertyValue> </NumValues> </PureOrMixtureData> </DataReport>

Right click here and Save Target to download the xml file

Information on ThermoML