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<?xml version="1.0" encoding="UTF-8"?> <!--Created by Guided Data Capture (GDC) Software (http://www.trc.nist.gov)--> <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>let</sAuthor1> <sAuthor2>dee</sAuthor2> <nAuthorn>0</nAuthorn> </TRCRefID> <eType>journal</eType> <eSourceType>Original</eSourceType> <sAuthor>Letcher, T. M.[Trevor M.]</sAuthor> <sAuthor>Deenadayalu, N.[Nirmala]</sAuthor> <sAuthor>Soko, B.[Bathabile]</sAuthor> <sAuthor>Ramjugernath, D.[Deresh]</sAuthor> <sAuthor>Naicker, P. K.[Pavan K.]</sAuthor> <sPubName>J. Chem. Eng. Data</sPubName> <yrPubYr>2003</yrPubYr> <dateCit>2003-08-08</dateCit> <sTitle>Ternary Liquid-Liquid Equilibria for Mixtures of 1-Methyl-3-octylimidazolium Chloride + an Alkanol + an Alkane at 298.2 K and 1 bar</sTitle> <sAbstract>Ternary liquid-liquid equilibria for the mixtures (1-methyl-3-octylimidazolium chloride + an alkanol + an alkane) at 298.2 K are reported. The alkanes used were heptane, dodecane, and hexadecane, and the alkanols were methanol and ethanol. The solubility of the alkanol is higher in the ionic liquid rich phase than in the alkane rich phase. The effectiveness of extracting an alkanol from mixtures containing an alkane using the solvent 1-methyl-3-octylimidazolium chloride is discussed in terms of the ratio of the solubilities in the two phases. The NRTL equation was used to correlate the experimental tie lines. There are no data in the literature for the mixtures discussed in this paper.</sAbstract> <sKeyword>ternary liquid-liquid equilibria</sKeyword> <sKeyword>1-methyl-3-octylimidazolium chloride</sKeyword> <sKeyword>heptane</sKeyword> <sKeyword>dodecane</sKeyword> <sKeyword>hexadecane</sKeyword> <sKeyword>methanol</sKeyword> <sKeyword>ethanol,</sKeyword> <sVol>48</sVol> <sPage>904-907</sPage> </Citation> <Compound> <RegNum> <nOrgNum>1</nOrgNum> </RegNum> <sCommonName>1-methyl-3-octylimidazolium chloride</sCommonName> <sFormulaMolec>C12H23ClN2</sFormulaMolec> <Sample> <nSampleNm>1</nSampleNm> <eSource>Commercial source</eSource> <purity> <nStep>1</nStep> <nPurityMass>98</nPurityMass> <nPurityMassDigits>2</nPurityMassDigits> <eAnalMeth>Not known</eAnalMeth> </purity> <purity> <nStep>2</nStep> <ePurifMethod>Dried by vacuum heating</ePurifMethod> </purity> </Sample> </Compound> <Compound> <RegNum> <nOrgNum>2</nOrgNum> </RegNum> <sCommonName>hexadecane</sCommonName> <sFormulaMolec>C16H34</sFormulaMolec> <Sample> <nSampleNm>1</nSampleNm> <eSource>Commercial source</eSource> <purity> <nStep>1</nStep> <nPurityMass>99</nPurityMass> <nPurityMassDigits>2</nPurityMassDigits> <eAnalMeth>Gas chromatography</eAnalMeth> </purity> <purity> <nStep>2</nStep> <ePurifMethod>None used</ePurifMethod> </purity> </Sample> </Compound> <Compound> <RegNum> <nOrgNum>3</nOrgNum> </RegNum> <sCommonName>dodecane</sCommonName> <sFormulaMolec>C12H26</sFormulaMolec> <Sample> <nSampleNm>1</nSampleNm> <eSource>Commercial source</eSource> <purity> <nStep>1</nStep> <nPurityMass>99</nPurityMass> <nPurityMassDigits>2</nPurityMassDigits> <eAnalMeth>Gas chromatography</eAnalMeth> </purity> <purity> <nStep>2</nStep> <ePurifMethod>None used</ePurifMethod> </purity> </Sample> </Compound> <Compound> <RegNum> <nOrgNum>4</nOrgNum> </RegNum> <sCommonName>heptane</sCommonName> <sFormulaMolec>C7H16</sFormulaMolec> <Sample> <nSampleNm>1</nSampleNm> <eSource>Commercial source</eSource> <purity> <nStep>1</nStep> <nPurityMass>99</nPurityMass> <nPurityMassDigits>2</nPurityMassDigits> <eAnalMeth>Gas chromatography</eAnalMeth> </purity> <purity> <nStep>2</nStep> <ePurifMethod>None used</ePurifMethod> </purity> </Sample> </Compound> <Compound> <RegNum> <nOrgNum>5</nOrgNum> </RegNum> <sCommonName>methanol</sCommonName> <sFormulaMolec>CH4O</sFormulaMolec> <Sample> <nSampleNm>1</nSampleNm> <eSource>Commercial source</eSource> <purity> <nStep>1</nStep> <nPurityMass>99</nPurityMass> <nPurityMassDigits>2</nPurityMassDigits> <eAnalMeth>Gas chromatography</eAnalMeth> </purity> <purity> <nStep>2</nStep> <ePurifMethod>Molecular sieve treatment</ePurifMethod> </purity> </Sample> </Compound> <Compound> <RegNum> <nOrgNum>6</nOrgNum> </RegNum> <sCommonName>ethanol</sCommonName> <sFormulaMolec>C2H6O</sFormulaMolec> <Sample> <nSampleNm>1</nSampleNm> <eSource>Commercial source</eSource> <purity> <nStep>1</nStep> <nPurityMass>99</nPurityMass> <nPurityMassDigits>2</nPurityMassDigits> <eAnalMeth>Gas chromatography</eAnalMeth> </purity> <purity> <nStep>2</nStep> <ePurifMethod>Molecular sieve treatment</ePurifMethod> </purity> </Sample> </Compound> <PureOrMixtureData> <Component> <RegNum> <nOrgNum>1</nOrgNum> </RegNum> <nSampleNm>1</nSampleNm> </Component> <eExpPurpose>Principal objective of the work</eExpPurpose> <sCompiler>MAS</sCompiler> <sContributor>TRC</sContributor> <dateDateAdded>8/6/2003</dateDateAdded> <Property> <nPropNumber>1</nPropNumber> <Property-MethodID> <PropertyGroup> <VolumetricProp> <ePropName>Mass density, kg/m3</ePropName> <eMethodName>Vibrating tube method</eMethodName> </VolumetricProp> </PropertyGroup> </Property-MethodID> <PropPhaseID> <ePropPhase>Liquid</ePropPhase> </PropPhaseID> <ePresentation>Direct value, X</ePresentation> </Property> <PhaseID> <ePhase>Liquid</ePhase> </PhaseID> <Constraint> <ConstraintID> <ConstraintType> <ePressure>Pressure, kPa</ePressure> </ConstraintType> </ConstraintID> <nConstraintValue>101.325</nConstraintValue> <nConstrDigits>6</nConstrDigits> </Constraint> <Variable> <nVarNumber>1</nVarNumber> <VariableID> <VariableType> <eTemperature>Temperature, K</eTemperature> </VariableType> </VariableID> </Variable> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>298.2</nVarValue> <nVarDigits>4</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>1010.4</nPropValue> <nPropDigits>5</nPropDigits> </PropertyValue> </NumValues> </PureOrMixtureData> <PureOrMixtureData> <Component> <RegNum> <nOrgNum>2</nOrgNum> </RegNum> <nSampleNm>1</nSampleNm> </Component> <eExpPurpose>Principal objective of the work</eExpPurpose> <sCompiler>MAS</sCompiler> <sContributor>TRC</sContributor> <dateDateAdded>8/6/2003</dateDateAdded> <Property> <nPropNumber>1</nPropNumber> <Property-MethodID> <PropertyGroup> <VolumetricProp> <ePropName>Mass density, kg/m3</ePropName> <eMethodName>Vibrating tube method</eMethodName> </VolumetricProp> </PropertyGroup> </Property-MethodID> <PropPhaseID> <ePropPhase>Liquid</ePropPhase> </PropPhaseID> <ePresentation>Direct value, X</ePresentation> </Property> <PhaseID> <ePhase>Liquid</ePhase> </PhaseID> <Constraint> <ConstraintID> <ConstraintType> <ePressure>Pressure, kPa</ePressure> </ConstraintType> </ConstraintID> <nConstraintValue>101.325</nConstraintValue> <nConstrDigits>6</nConstrDigits> </Constraint> <Variable> <nVarNumber>1</nVarNumber> <VariableID> <VariableType> <eTemperature>Temperature, K</eTemperature> </VariableType> </VariableID> </Variable> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>298.2</nVarValue> <nVarDigits>4</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>770.3</nPropValue> <nPropDigits>4</nPropDigits> </PropertyValue> </NumValues> </PureOrMixtureData> <PureOrMixtureData> <Component> <RegNum> <nOrgNum>3</nOrgNum> </RegNum> <nSampleNm>1</nSampleNm> </Component> <eExpPurpose>Principal objective of the work</eExpPurpose> <sCompiler>MAS</sCompiler> <sContributor>TRC</sContributor> <dateDateAdded>8/6/2003</dateDateAdded> <Property> <nPropNumber>1</nPropNumber> <Property-MethodID> <PropertyGroup> <VolumetricProp> <ePropName>Mass density, kg/m3</ePropName> <eMethodName>Vibrating tube method</eMethodName> </VolumetricProp> </PropertyGroup> </Property-MethodID> <PropPhaseID> <ePropPhase>Liquid</ePropPhase> </PropPhaseID> <ePresentation>Direct value, X</ePresentation> </Property> <PhaseID> <ePhase>Liquid</ePhase> </PhaseID> <Constraint> <ConstraintID> <ConstraintType> <ePressure>Pressure, kPa</ePressure> </ConstraintType> </ConstraintID> <nConstraintValue>101.325</nConstraintValue> <nConstrDigits>6</nConstrDigits> </Constraint> <Variable> <nVarNumber>1</nVarNumber> <VariableID> <VariableType> <eTemperature>Temperature, K</eTemperature> </VariableType> </VariableID> </Variable> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>298.2</nVarValue> <nVarDigits>4</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>746.6</nPropValue> <nPropDigits>4</nPropDigits> </PropertyValue> </NumValues> </PureOrMixtureData> <PureOrMixtureData> <Component> <RegNum> <nOrgNum>4</nOrgNum> </RegNum> <nSampleNm>1</nSampleNm> </Component> <eExpPurpose>Principal objective of the work</eExpPurpose> <sCompiler>MAS</sCompiler> <sContributor>TRC</sContributor> <dateDateAdded>8/6/2003</dateDateAdded> <Property> <nPropNumber>1</nPropNumber> <Property-MethodID> <PropertyGroup> <VolumetricProp> <ePropName>Mass density, kg/m3</ePropName> <eMethodName>Vibrating tube method</eMethodName> </VolumetricProp> </PropertyGroup> </Property-MethodID> <PropPhaseID> <ePropPhase>Liquid</ePropPhase> </PropPhaseID> <ePresentation>Direct value, X</ePresentation> </Property> <PhaseID> <ePhase>Liquid</ePhase> </PhaseID> <Constraint> <ConstraintID> <ConstraintType> <ePressure>Pressure, kPa</ePressure> </ConstraintType> </ConstraintID> <nConstraintValue>101.325</nConstraintValue> <nConstrDigits>6</nConstrDigits> </Constraint> <Variable> <nVarNumber>1</nVarNumber> <VariableID> <VariableType> <eTemperature>Temperature, K</eTemperature> </VariableType> </VariableID> </Variable> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>298.2</nVarValue> <nVarDigits>4</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>682.3</nPropValue> <nPropDigits>4</nPropDigits> </PropertyValue> </NumValues> </PureOrMixtureData> <PureOrMixtureData> <Component> <RegNum> <nOrgNum>5</nOrgNum> </RegNum> <nSampleNm>1</nSampleNm> </Component> <eExpPurpose>Principal objective of the work</eExpPurpose> <sCompiler>MAS</sCompiler> <sContributor>TRC</sContributor> <dateDateAdded>8/6/2003</dateDateAdded> <Property> <nPropNumber>1</nPropNumber> <Property-MethodID> <PropertyGroup> <VolumetricProp> <ePropName>Mass density, kg/m3</ePropName> <eMethodName>Vibrating tube method</eMethodName> </VolumetricProp> </PropertyGroup> </Property-MethodID> <PropPhaseID> <ePropPhase>Liquid</ePropPhase> </PropPhaseID> <ePresentation>Direct value, X</ePresentation> </Property> <PhaseID> <ePhase>Liquid</ePhase> </PhaseID> <Constraint> <ConstraintID> <ConstraintType> <ePressure>Pressure, kPa</ePressure> </ConstraintType> </ConstraintID> <nConstraintValue>101.325</nConstraintValue> <nConstrDigits>6</nConstrDigits> </Constraint> <Variable> <nVarNumber>1</nVarNumber> <VariableID> <VariableType> <eTemperature>Temperature, K</eTemperature> </VariableType> </VariableID> </Variable> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>298.2</nVarValue> <nVarDigits>4</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>786.27</nPropValue> <nPropDigits>5</nPropDigits> </PropertyValue> </NumValues> </PureOrMixtureData> <PureOrMixtureData> <Component> <RegNum> <nOrgNum>6</nOrgNum> </RegNum> <nSampleNm>1</nSampleNm> </Component> <eExpPurpose>Principal objective of the work</eExpPurpose> <sCompiler>MAS</sCompiler> <sContributor>TRC</sContributor> <dateDateAdded>8/6/2003</dateDateAdded> <Property> <nPropNumber>1</nPropNumber> <Property-MethodID> <PropertyGroup> <VolumetricProp> <ePropName>Mass density, kg/m3</ePropName> <eMethodName>Vibrating tube method</eMethodName> </VolumetricProp> </PropertyGroup> </Property-MethodID> <PropPhaseID> <ePropPhase>Liquid</ePropPhase> </PropPhaseID> <ePresentation>Direct value, X</ePresentation> </Property> <PhaseID> <ePhase>Liquid</ePhase> </PhaseID> <Constraint> <ConstraintID> <ConstraintType> <ePressure>Pressure, kPa</ePressure> </ConstraintType> </ConstraintID> <nConstraintValue>101.325</nConstraintValue> <nConstrDigits>6</nConstrDigits> </Constraint> <Variable> <nVarNumber>1</nVarNumber> <VariableID> <VariableType> <eTemperature>Temperature, K</eTemperature> </VariableType> </VariableID> </Variable> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>298.2</nVarValue> <nVarDigits>4</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>784.93</nPropValue> <nPropDigits>5</nPropDigits> </PropertyValue> </NumValues> </PureOrMixtureData> <PureOrMixtureData> <Component> <RegNum> <nOrgNum>5</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>MAS</sCompiler> <sContributor>TRC</sContributor> <dateDateAdded>8/7/2003</dateDateAdded> <Property> <nPropNumber>1</nPropNumber> <Property-MethodID> <PropertyGroup> <CompositionAtPhaseEquilibrium> <ePropName>Mole fraction</ePropName> <eMethodName>Titration method</eMethodName> </CompositionAtPhaseEquilibrium> </PropertyGroup> <RegNum> <nOrgNum>5</nOrgNum> </RegNum> </Property-MethodID> <PropPhaseID> <ePropPhase>Liquid mixture 1</ePropPhase> </PropPhaseID> <ePresentation>Direct value, X</ePresentation> </Property> <PhaseID> <ePhase>Liquid mixture 1</ePhase> </PhaseID> <PhaseID> <ePhase>Liquid mixture 2</ePhase> </PhaseID> <Constraint> <ConstraintID> <ConstraintType> <eTemperature>Temperature, K</eTemperature> </ConstraintType> </ConstraintID> <nConstraintValue>298.2</nConstraintValue> <nConstrDigits>4</nConstrDigits> </Constraint> <Constraint> <ConstraintID> <ConstraintType> <ePressure>Pressure, kPa</ePressure> </ConstraintType> </ConstraintID> <nConstraintValue>100</nConstraintValue> <nConstrDigits>3</nConstrDigits> </Constraint> <Variable> <nVarNumber>1</nVarNumber> <VariableID> <VariableType> <eComponentComposition>Mole fraction</eComponentComposition> </VariableType> <RegNum> <nOrgNum>1</nOrgNum> </RegNum> </VariableID> <VarPhaseID> <eVarPhase>Liquid mixture 1</eVarPhase> </VarPhaseID> </Variable> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>0</nVarValue> <nVarDigits>0</nVarDigits> </VariableValue> <PropertyValue> 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</PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.935</nVarValue> <nVarDigits>3</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>0</nPropValue> <nPropDigits>0</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.007</nVarValue> <nVarDigits>1</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>0</nPropValue> <nPropDigits>0</nPropDigits> </PropertyValue> </NumValues> </PureOrMixtureData> <PureOrMixtureData> <Component> <RegNum> <nOrgNum>5</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>RDC</sCompiler> <sContributor>TRC</sContributor> 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<nOrgNum>1</nOrgNum> </RegNum> </VariableID> <VarPhaseID> <eVarPhase>Liquid mixture 1</eVarPhase> </VarPhaseID> </Variable> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.183</nVarValue> <nVarDigits>3</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>.728</nPropValue> <nPropDigits>3</nPropDigits> </PropertyValue> <PropertyValue> <nPropNumber>2</nPropNumber> <nPropValue>.02</nPropValue> <nPropDigits>2</nPropDigits> </PropertyValue> <PropertyValue> <nPropNumber>3</nPropNumber> <nPropValue>0</nPropValue> <nPropDigits>0</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.463</nVarValue> <nVarDigits>3</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>.447</nPropValue> <nPropDigits>3</nPropDigits> </PropertyValue> <PropertyValue> <nPropNumber>2</nPropNumber> <nPropValue>.001</nPropValue> <nPropDigits>1</nPropDigits> </PropertyValue> <PropertyValue> <nPropNumber>3</nPropNumber> <nPropValue>0</nPropValue> <nPropDigits>0</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.546</nVarValue> <nVarDigits>3</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>.365</nPropValue> <nPropDigits>3</nPropDigits> </PropertyValue> <PropertyValue> <nPropNumber>2</nPropNumber> <nPropValue>.0005</nPropValue> <nPropDigits>1</nPropDigits> </PropertyValue> <PropertyValue> <nPropNumber>3</nPropNumber> <nPropValue>.001</nPropValue> <nPropDigits>1</nPropDigits> </PropertyValue> </NumValues> </PureOrMixtureData> <PureOrMixtureData> <Component> <RegNum> <nOrgNum>5</nOrgNum> </RegNum> <nSampleNm>1</nSampleNm> </Component> <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>MAS</sCompiler> <sContributor>TRC</sContributor> <dateDateAdded>8/7/2003</dateDateAdded> <Property> <nPropNumber>1</nPropNumber> <Property-MethodID> <PropertyGroup> <CompositionAtPhaseEquilibrium> <ePropName>Mole fraction</ePropName> <eMethodName>Titration method</eMethodName> </CompositionAtPhaseEquilibrium> </PropertyGroup> <RegNum> <nOrgNum>5</nOrgNum> </RegNum> </Property-MethodID> <PropPhaseID> <ePropPhase>Liquid mixture 1</ePropPhase> </PropPhaseID> <ePresentation>Direct value, X</ePresentation> </Property> <PhaseID> <ePhase>Liquid mixture 1</ePhase> </PhaseID> <PhaseID> <ePhase>Liquid mixture 2</ePhase> </PhaseID> <Constraint> <ConstraintID> <ConstraintType> <eTemperature>Temperature, K</eTemperature> </ConstraintType> </ConstraintID> <nConstraintValue>298.2</nConstraintValue> <nConstrDigits>4</nConstrDigits> </Constraint> <Constraint> <ConstraintID> <ConstraintType> <ePressure>Pressure, kPa</ePressure> </ConstraintType> </ConstraintID> <nConstraintValue>100</nConstraintValue> <nConstrDigits>3</nConstrDigits> </Constraint> <Variable> <nVarNumber>1</nVarNumber> <VariableID> <VariableType> <eComponentComposition>Mole fraction</eComponentComposition> </VariableType> <RegNum> <nOrgNum>1</nOrgNum> </RegNum> </VariableID> <VarPhaseID> <eVarPhase>Liquid mixture 1</eVarPhase> </VarPhaseID> </Variable> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>0</nVarValue> <nVarDigits>0</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>.008</nPropValue> <nPropDigits>1</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.01</nVarValue> <nVarDigits>2</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>0</nPropValue> <nPropDigits>0</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.1</nVarValue> <nVarDigits>3</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>.898</nPropValue> <nPropDigits>3</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.139</nVarValue> <nVarDigits>3</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>.859</nPropValue> <nPropDigits>3</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.245</nVarValue> <nVarDigits>3</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>.75</nPropValue> <nPropDigits>3</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.295</nVarValue> <nVarDigits>3</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>.7</nPropValue> <nPropDigits>3</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.411</nVarValue> <nVarDigits>3</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>.582</nPropValue> <nPropDigits>3</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.492</nVarValue> <nVarDigits>3</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>.501</nPropValue> <nPropDigits>3</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.69</nVarValue> <nVarDigits>3</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>.297</nPropValue> <nPropDigits>3</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.712</nVarValue> <nVarDigits>3</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>.278</nPropValue> <nPropDigits>3</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.873</nVarValue> <nVarDigits>3</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>.111</nPropValue> <nPropDigits>3</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.903</nVarValue> <nVarDigits>3</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>.078</nPropValue> <nPropDigits>2</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.981</nVarValue> <nVarDigits>3</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>0</nPropValue> <nPropDigits>0</nPropDigits> </PropertyValue> </NumValues> </PureOrMixtureData> <PureOrMixtureData> <Component> <RegNum> <nOrgNum>5</nOrgNum> </RegNum> <nSampleNm>1</nSampleNm> </Component> <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>8/7/2003</dateDateAdded> <Property> <nPropNumber>1</nPropNumber> <Property-MethodID> <PropertyGroup> <CompositionAtPhaseEquilibrium> <ePropName>Mole fraction</ePropName> <eMethodName>Other</eMethodName> </CompositionAtPhaseEquilibrium> </PropertyGroup> <RegNum> <nOrgNum>5</nOrgNum> </RegNum> </Property-MethodID> <PropPhaseID> <ePropPhase>Liquid mixture 1</ePropPhase> </PropPhaseID> <ePresentation>Direct value, X</ePresentation> </Property> <Property> <nPropNumber>2</nPropNumber> <Property-MethodID> <PropertyGroup> <CompositionAtPhaseEquilibrium> <ePropName>Mole fraction</ePropName> <eMethodName>Other</eMethodName> </CompositionAtPhaseEquilibrium> </PropertyGroup> <RegNum> <nOrgNum>1</nOrgNum> </RegNum> </Property-MethodID> <PropPhaseID> <ePropPhase>Liquid mixture 2</ePropPhase> </PropPhaseID> <ePresentation>Direct value, X</ePresentation> </Property> <Property> <nPropNumber>3</nPropNumber> <Property-MethodID> <PropertyGroup> <CompositionAtPhaseEquilibrium> <ePropName>Mole fraction</ePropName> <eMethodName>Other</eMethodName> </CompositionAtPhaseEquilibrium> </PropertyGroup> <RegNum> <nOrgNum>5</nOrgNum> </RegNum> </Property-MethodID> <PropPhaseID> <ePropPhase>Liquid mixture 2</ePropPhase> </PropPhaseID> <ePresentation>Direct value, X</ePresentation> </Property> <PhaseID> <ePhase>Liquid mixture 1</ePhase> </PhaseID> <PhaseID> <ePhase>Liquid mixture 2</ePhase> </PhaseID> <Constraint> <ConstraintID> <ConstraintType> <eTemperature>Temperature, K</eTemperature> </ConstraintType> </ConstraintID> <nConstraintValue>298.15</nConstraintValue> <nConstrDigits>5</nConstrDigits> </Constraint> <Constraint> <ConstraintID> <ConstraintType> <ePressure>Pressure, kPa</ePressure> </ConstraintType> </ConstraintID> <nConstraintValue>101.3</nConstraintValue> <nConstrDigits>4</nConstrDigits> </Constraint> <Variable> <nVarNumber>1</nVarNumber> <VariableID> <VariableType> <eComponentComposition>Mole fraction</eComponentComposition> </VariableType> <RegNum> <nOrgNum>1</nOrgNum> </RegNum> </VariableID> <VarPhaseID> <eVarPhase>Liquid mixture 1</eVarPhase> </VarPhaseID> </Variable> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.873</nVarValue> <nVarDigits>3</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>.111</nPropValue> <nPropDigits>3</nPropDigits> </PropertyValue> <PropertyValue> <nPropNumber>2</nPropNumber> <nPropValue>.001</nPropValue> <nPropDigits>1</nPropDigits> </PropertyValue> <PropertyValue> <nPropNumber>3</nPropNumber> <nPropValue>.0003</nPropValue> <nPropDigits>1</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.69</nVarValue> <nVarDigits>3</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>.297</nPropValue> <nPropDigits>3</nPropDigits> </PropertyValue> <PropertyValue> <nPropNumber>2</nPropNumber> <nPropValue>.001</nPropValue> <nPropDigits>1</nPropDigits> </PropertyValue> <PropertyValue> <nPropNumber>3</nPropNumber> <nPropValue>.0003</nPropValue> <nPropDigits>1</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.411</nVarValue> <nVarDigits>3</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>.582</nPropValue> <nPropDigits>3</nPropDigits> </PropertyValue> <PropertyValue> <nPropNumber>2</nPropNumber> <nPropValue>.001</nPropValue> <nPropDigits>1</nPropDigits> </PropertyValue> <PropertyValue> <nPropNumber>3</nPropNumber> <nPropValue>.0003</nPropValue> <nPropDigits>1</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.245</nVarValue> <nVarDigits>3</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>.75</nPropValue> <nPropDigits>3</nPropDigits> </PropertyValue> <PropertyValue> <nPropNumber>2</nPropNumber> <nPropValue>.001</nPropValue> <nPropDigits>1</nPropDigits> </PropertyValue> <PropertyValue> <nPropNumber>3</nPropNumber> <nPropValue>.0003</nPropValue> <nPropDigits>1</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.139</nVarValue> <nVarDigits>3</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>.859</nPropValue> <nPropDigits>3</nPropDigits> </PropertyValue> <PropertyValue> <nPropNumber>2</nPropNumber> <nPropValue>.0004</nPropValue> <nPropDigits>1</nPropDigits> </PropertyValue> <PropertyValue> <nPropNumber>3</nPropNumber> <nPropValue>.0006</nPropValue> <nPropDigits>1</nPropDigits> </PropertyValue> </NumValues> </PureOrMixtureData> <PureOrMixtureData> <Component> <RegNum> <nOrgNum>6</nOrgNum> </RegNum> <nSampleNm>1</nSampleNm> </Component> <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>MAS</sCompiler> <sContributor>TRC</sContributor> <dateDateAdded>8/7/2003</dateDateAdded> <Property> <nPropNumber>1</nPropNumber> <Property-MethodID> <PropertyGroup> <CompositionAtPhaseEquilibrium> <ePropName>Mole fraction</ePropName> <eMethodName>Titration method</eMethodName> </CompositionAtPhaseEquilibrium> </PropertyGroup> <RegNum> <nOrgNum>6</nOrgNum> </RegNum> </Property-MethodID> <PropPhaseID> <ePropPhase>Liquid mixture 1</ePropPhase> </PropPhaseID> <ePresentation>Direct value, X</ePresentation> </Property> <PhaseID> <ePhase>Liquid mixture 1</ePhase> </PhaseID> <PhaseID> <ePhase>Liquid mixture 2</ePhase> </PhaseID> <Constraint> <ConstraintID> <ConstraintType> <eTemperature>Temperature, K</eTemperature> </ConstraintType> </ConstraintID> <nConstraintValue>298.2</nConstraintValue> <nConstrDigits>4</nConstrDigits> </Constraint> <Constraint> <ConstraintID> <ConstraintType> <ePressure>Pressure, kPa</ePressure> </ConstraintType> </ConstraintID> <nConstraintValue>100</nConstraintValue> <nConstrDigits>3</nConstrDigits> </Constraint> <Variable> <nVarNumber>1</nVarNumber> <VariableID> <VariableType> <eComponentComposition>Mole fraction</eComponentComposition> </VariableType> <RegNum> <nOrgNum>1</nOrgNum> </RegNum> </VariableID> <VarPhaseID> <eVarPhase>Liquid mixture 1</eVarPhase> </VarPhaseID> </Variable> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>0</nVarValue> <nVarDigits>0</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>.956</nPropValue> <nPropDigits>3</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.01</nVarValue> <nVarDigits>2</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>0</nPropValue> <nPropDigits>0</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.097</nVarValue> <nVarDigits>2</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>.876</nPropValue> <nPropDigits>3</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.125</nVarValue> <nVarDigits>3</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>.846</nPropValue> <nPropDigits>3</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.221</nVarValue> <nVarDigits>3</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>.758</nPropValue> <nPropDigits>3</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.279</nVarValue> <nVarDigits>3</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>.709</nPropValue> <nPropDigits>3</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.291</nVarValue> <nVarDigits>3</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>.693</nPropValue> <nPropDigits>3</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.306</nVarValue> <nVarDigits>3</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>.679</nPropValue> <nPropDigits>3</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.451</nVarValue> <nVarDigits>3</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>.538</nPropValue> <nPropDigits>3</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.459</nVarValue> <nVarDigits>3</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>.532</nPropValue> <nPropDigits>3</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.48</nVarValue> <nVarDigits>3</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>.513</nPropValue> <nPropDigits>3</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.543</nVarValue> <nVarDigits>3</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>.449</nPropValue> <nPropDigits>3</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.586</nVarValue> <nVarDigits>3</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>.407</nPropValue> <nPropDigits>3</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.599</nVarValue> <nVarDigits>3</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>.396</nPropValue> <nPropDigits>3</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.981</nVarValue> <nVarDigits>3</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>0</nPropValue> <nPropDigits>0</nPropDigits> </PropertyValue> </NumValues> </PureOrMixtureData> <PureOrMixtureData> <Component> <RegNum> <nOrgNum>6</nOrgNum> </RegNum> <nSampleNm>1</nSampleNm> </Component> <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>8/7/2003</dateDateAdded> <Property> <nPropNumber>1</nPropNumber> <Property-MethodID> <PropertyGroup> <CompositionAtPhaseEquilibrium> <ePropName>Mole fraction</ePropName> <eMethodName>Other</eMethodName> </CompositionAtPhaseEquilibrium> </PropertyGroup> <RegNum> <nOrgNum>6</nOrgNum> </RegNum> </Property-MethodID> <PropPhaseID> <ePropPhase>Liquid mixture 1</ePropPhase> </PropPhaseID> <ePresentation>Direct value, X</ePresentation> </Property> <Property> <nPropNumber>2</nPropNumber> <Property-MethodID> <PropertyGroup> <CompositionAtPhaseEquilibrium> <ePropName>Mole fraction</ePropName> <eMethodName>Other</eMethodName> </CompositionAtPhaseEquilibrium> </PropertyGroup> <RegNum> <nOrgNum>6</nOrgNum> </RegNum> </Property-MethodID> <PropPhaseID> <ePropPhase>Liquid mixture 2</ePropPhase> </PropPhaseID> <ePresentation>Direct value, X</ePresentation> </Property> <Property> <nPropNumber>3</nPropNumber> <Property-MethodID> <PropertyGroup> <CompositionAtPhaseEquilibrium> <ePropName>Mole fraction</ePropName> <eMethodName>Other</eMethodName> </CompositionAtPhaseEquilibrium> </PropertyGroup> <RegNum> <nOrgNum>1</nOrgNum> </RegNum> </Property-MethodID> <PropPhaseID> <ePropPhase>Liquid mixture 2</ePropPhase> </PropPhaseID> <ePresentation>Direct value, X</ePresentation> </Property> <PhaseID> <ePhase>Liquid mixture 1</ePhase> </PhaseID> <PhaseID> <ePhase>Liquid mixture 2</ePhase> </PhaseID> <Constraint> <ConstraintID> <ConstraintType> <ePressure>Pressure, kPa</ePressure> </ConstraintType> </ConstraintID> <nConstraintValue>101.3</nConstraintValue> <nConstrDigits>4</nConstrDigits> </Constraint> <Constraint> <ConstraintID> <ConstraintType> <eTemperature>Temperature, K</eTemperature> </ConstraintType> </ConstraintID> <nConstraintValue>298.2</nConstraintValue> <nConstrDigits>4</nConstrDigits> </Constraint> <Variable> <nVarNumber>1</nVarNumber> <VariableID> <VariableType> <eComponentComposition>Mole fraction</eComponentComposition> </VariableType> <RegNum> <nOrgNum>1</nOrgNum> </RegNum> </VariableID> <VarPhaseID> <eVarPhase>Liquid mixture 1</eVarPhase> </VarPhaseID> </Variable> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.125</nVarValue> <nVarDigits>3</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>.846</nPropValue> <nPropDigits>3</nPropDigits> </PropertyValue> <PropertyValue> <nPropNumber>2</nPropNumber> <nPropValue>.002</nPropValue> <nPropDigits>1</nPropDigits> </PropertyValue> <PropertyValue> <nPropNumber>3</nPropNumber> <nPropValue>.001</nPropValue> <nPropDigits>1</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.221</nVarValue> <nVarDigits>3</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>.758</nPropValue> <nPropDigits>3</nPropDigits> </PropertyValue> <PropertyValue> <nPropNumber>2</nPropNumber> <nPropValue>.002</nPropValue> <nPropDigits>1</nPropDigits> </PropertyValue> <PropertyValue> <nPropNumber>3</nPropNumber> <nPropValue>0</nPropValue> <nPropDigits>0</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.306</nVarValue> <nVarDigits>3</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>.679</nPropValue> <nPropDigits>3</nPropDigits> </PropertyValue> <PropertyValue> <nPropNumber>2</nPropNumber> <nPropValue>.001</nPropValue> <nPropDigits>1</nPropDigits> </PropertyValue> <PropertyValue> <nPropNumber>3</nPropNumber> <nPropValue>.001</nPropValue> <nPropDigits>1</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.46</nVarValue> <nVarDigits>3</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>.532</nPropValue> <nPropDigits>3</nPropDigits> </PropertyValue> <PropertyValue> <nPropNumber>2</nPropNumber> <nPropValue>0</nPropValue> <nPropDigits>0</nPropDigits> </PropertyValue> <PropertyValue> <nPropNumber>3</nPropNumber> <nPropValue>.001</nPropValue> <nPropDigits>1</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.587</nVarValue> <nVarDigits>3</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>.407</nPropValue> <nPropDigits>3</nPropDigits> </PropertyValue> <PropertyValue> <nPropNumber>2</nPropNumber> <nPropValue>0</nPropValue> <nPropDigits>0</nPropDigits> </PropertyValue> <PropertyValue> <nPropNumber>3</nPropNumber> <nPropValue>.001</nPropValue> <nPropDigits>1</nPropDigits> </PropertyValue> </NumValues> </PureOrMixtureData> <PureOrMixtureData> <Component> <RegNum> <nOrgNum>6</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>MAS</sCompiler> <sContributor>TRC</sContributor> <dateDateAdded>8/7/2003</dateDateAdded> <Property> <nPropNumber>1</nPropNumber> <Property-MethodID> <PropertyGroup> <CompositionAtPhaseEquilibrium> <ePropName>Mole fraction</ePropName> <eMethodName>Titration method</eMethodName> </CompositionAtPhaseEquilibrium> </PropertyGroup> <RegNum> <nOrgNum>6</nOrgNum> </RegNum> </Property-MethodID> <PropPhaseID> <ePropPhase>Liquid mixture 1</ePropPhase> </PropPhaseID> <ePresentation>Direct value, X</ePresentation> </Property> <PhaseID> <ePhase>Liquid mixture 1</ePhase> </PhaseID> <PhaseID> <ePhase>Liquid mixture 2</ePhase> </PhaseID> <Constraint> <ConstraintID> <ConstraintType> <eTemperature>Temperature, K</eTemperature> </ConstraintType> </ConstraintID> <nConstraintValue>298.2</nConstraintValue> <nConstrDigits>4</nConstrDigits> </Constraint> <Constraint> <ConstraintID> <ConstraintType> <ePressure>Pressure, kPa</ePressure> </ConstraintType> </ConstraintID> <nConstraintValue>100</nConstraintValue> <nConstrDigits>3</nConstrDigits> </Constraint> <Variable> <nVarNumber>1</nVarNumber> <VariableID> <VariableType> <eComponentComposition>Mole fraction</eComponentComposition> </VariableType> <RegNum> <nOrgNum>1</nOrgNum> </RegNum> </VariableID> <VarPhaseID> <eVarPhase>Liquid mixture 1</eVarPhase> </VarPhaseID> </Variable> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.009</nVarValue> <nVarDigits>1</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>0</nPropValue> <nPropDigits>0</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.008</nVarValue> <nVarDigits>1</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>.535</nPropValue> <nPropDigits>3</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.027</nVarValue> <nVarDigits>2</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>.875</nPropValue> <nPropDigits>3</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.077</nVarValue> <nVarDigits>2</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>.86</nPropValue> <nPropDigits>3</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.098</nVarValue> <nVarDigits>2</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>.859</nPropValue> <nPropDigits>3</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.14</nVarValue> <nVarDigits>3</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>.81</nPropValue> <nPropDigits>3</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.27</nVarValue> <nVarDigits>3</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>.684</nPropValue> <nPropDigits>3</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.286</nVarValue> <nVarDigits>3</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>.672</nPropValue> <nPropDigits>3</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.315</nVarValue> <nVarDigits>3</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>.651</nPropValue> <nPropDigits>3</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.43</nVarValue> <nVarDigits>3</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>.532</nPropValue> <nPropDigits>3</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.481</nVarValue> <nVarDigits>3</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>.482</nPropValue> <nPropDigits>3</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.5</nVarValue> <nVarDigits>3</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>.478</nPropValue> <nPropDigits>3</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.694</nVarValue> <nVarDigits>3</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>.294</nPropValue> <nPropDigits>3</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.89</nVarValue> <nVarDigits>3</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>.009</nPropValue> <nPropDigits>1</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.923</nVarValue> <nVarDigits>3</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>.064</nPropValue> <nPropDigits>2</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.976</nVarValue> <nVarDigits>3</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>0</nPropValue> <nPropDigits>0</nPropDigits> </PropertyValue> </NumValues> </PureOrMixtureData> <PureOrMixtureData> <Component> <RegNum> <nOrgNum>6</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>RDC</sCompiler> <sContributor>TRC</sContributor> <dateDateAdded>8/7/2003</dateDateAdded> <Property> <nPropNumber>1</nPropNumber> <Property-MethodID> <PropertyGroup> <CompositionAtPhaseEquilibrium> <ePropName>Mole fraction</ePropName> <eMethodName>Other</eMethodName> </CompositionAtPhaseEquilibrium> </PropertyGroup> <RegNum> <nOrgNum>6</nOrgNum> </RegNum> </Property-MethodID> <PropPhaseID> <ePropPhase>Liquid mixture 1</ePropPhase> </PropPhaseID> <ePresentation>Direct value, X</ePresentation> </Property> <Property> <nPropNumber>2</nPropNumber> <Property-MethodID> <PropertyGroup> <CompositionAtPhaseEquilibrium> <ePropName>Mole fraction</ePropName> <eMethodName>Other</eMethodName> </CompositionAtPhaseEquilibrium> </PropertyGroup> <RegNum> <nOrgNum>6</nOrgNum> </RegNum> </Property-MethodID> <PropPhaseID> <ePropPhase>Liquid mixture 2</ePropPhase> </PropPhaseID> <ePresentation>Direct value, X</ePresentation> </Property> <Property> <nPropNumber>3</nPropNumber> <Property-MethodID> <PropertyGroup> <CompositionAtPhaseEquilibrium> <ePropName>Mole fraction</ePropName> <eMethodName>Other</eMethodName> </CompositionAtPhaseEquilibrium> </PropertyGroup> <RegNum> <nOrgNum>1</nOrgNum> </RegNum> </Property-MethodID> <PropPhaseID> <ePropPhase>Liquid mixture 2</ePropPhase> </PropPhaseID> <ePresentation>Direct value, X</ePresentation> </Property> <PhaseID> <ePhase>Liquid mixture 1</ePhase> </PhaseID> <PhaseID> <ePhase>Liquid mixture 2</ePhase> </PhaseID> <Constraint> <ConstraintID> <ConstraintType> <ePressure>Pressure, kPa</ePressure> </ConstraintType> </ConstraintID> <nConstraintValue>101.3</nConstraintValue> <nConstrDigits>4</nConstrDigits> </Constraint> <Constraint> <ConstraintID> <ConstraintType> <eTemperature>Temperature, K</eTemperature> </ConstraintType> </ConstraintID> <nConstraintValue>298.2</nConstraintValue> <nConstrDigits>4</nConstrDigits> </Constraint> <Variable> <nVarNumber>1</nVarNumber> <VariableID> <VariableType> <eComponentComposition>Mole fraction</eComponentComposition> </VariableType> <RegNum> <nOrgNum>1</nOrgNum> </RegNum> </VariableID> <VarPhaseID> <eVarPhase>Liquid mixture 1</eVarPhase> </VarPhaseID> </Variable> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.923</nVarValue> <nVarDigits>3</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>.064</nPropValue> <nPropDigits>2</nPropDigits> </PropertyValue> <PropertyValue> <nPropNumber>2</nPropNumber> <nPropValue>.006</nPropValue> <nPropDigits>1</nPropDigits> </PropertyValue> <PropertyValue> <nPropNumber>3</nPropNumber> <nPropValue>.001</nPropValue> <nPropDigits>1</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.43</nVarValue> <nVarDigits>3</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>.532</nPropValue> <nPropDigits>3</nPropDigits> </PropertyValue> <PropertyValue> <nPropNumber>2</nPropNumber> <nPropValue>.007</nPropValue> <nPropDigits>1</nPropDigits> </PropertyValue> <PropertyValue> <nPropNumber>3</nPropNumber> <nPropValue>.001</nPropValue> <nPropDigits>1</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.27</nVarValue> <nVarDigits>3</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>.684</nPropValue> <nPropDigits>3</nPropDigits> </PropertyValue> <PropertyValue> <nPropNumber>2</nPropNumber> <nPropValue>.007</nPropValue> <nPropDigits>1</nPropDigits> </PropertyValue> <PropertyValue> <nPropNumber>3</nPropNumber> <nPropValue>.001</nPropValue> <nPropDigits>1</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.14</nVarValue> <nVarDigits>3</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>.81</nPropValue> <nPropDigits>3</nPropDigits> </PropertyValue> <PropertyValue> <nPropNumber>2</nPropNumber> <nPropValue>.008</nPropValue> <nPropDigits>1</nPropDigits> </PropertyValue> <PropertyValue> <nPropNumber>3</nPropNumber> <nPropValue>.002</nPropValue> <nPropDigits>1</nPropDigits> </PropertyValue> </NumValues> </PureOrMixtureData> <PureOrMixtureData> <Component> <RegNum> <nOrgNum>6</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>MAS</sCompiler> <sContributor>TRC</sContributor> <dateDateAdded>8/7/2003</dateDateAdded> <Property> <nPropNumber>1</nPropNumber> <Property-MethodID> <PropertyGroup> <CompositionAtPhaseEquilibrium> <ePropName>Mole fraction</ePropName> <eMethodName>Titration method</eMethodName> </CompositionAtPhaseEquilibrium> </PropertyGroup> <RegNum> <nOrgNum>6</nOrgNum> </RegNum> </Property-MethodID> <PropPhaseID> <ePropPhase>Liquid mixture 1</ePropPhase> </PropPhaseID> <ePresentation>Direct value, X</ePresentation> </Property> <PhaseID> <ePhase>Liquid mixture 1</ePhase> </PhaseID> <PhaseID> <ePhase>Liquid mixture 2</ePhase> </PhaseID> <Constraint> <ConstraintID> <ConstraintType> <eTemperature>Temperature, K</eTemperature> </ConstraintType> </ConstraintID> <nConstraintValue>298.2</nConstraintValue> <nConstrDigits>4</nConstrDigits> </Constraint> <Constraint> <ConstraintID> <ConstraintType> <ePressure>Pressure, kPa</ePressure> </ConstraintType> </ConstraintID> <nConstraintValue>100</nConstraintValue> <nConstrDigits>3</nConstrDigits> </Constraint> <Variable> <nVarNumber>1</nVarNumber> <VariableID> <VariableType> <eComponentComposition>Mole fraction</eComponentComposition> </VariableType> <RegNum> <nOrgNum>1</nOrgNum> </RegNum> </VariableID> <VarPhaseID> <eVarPhase>Liquid mixture 1</eVarPhase> </VarPhaseID> </Variable> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.007</nVarValue> <nVarDigits>1</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>0</nPropValue> <nPropDigits>0</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.007</nVarValue> <nVarDigits>1</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>.007</nPropValue> <nPropDigits>1</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.007</nVarValue> <nVarDigits>1</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>.003</nPropValue> <nPropDigits>1</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.029</nVarValue> <nVarDigits>2</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>.489</nPropValue> <nPropDigits>3</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.062</nVarValue> <nVarDigits>2</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>.678</nPropValue> <nPropDigits>3</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.264</nVarValue> <nVarDigits>3</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>.574</nPropValue> <nPropDigits>3</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.306</nVarValue> <nVarDigits>3</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>.536</nPropValue> <nPropDigits>3</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.36</nVarValue> <nVarDigits>3</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>.489</nPropValue> <nPropDigits>3</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.454</nVarValue> <nVarDigits>3</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>.4</nPropValue> <nPropDigits>3</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.493</nVarValue> <nVarDigits>3</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>.371</nPropValue> <nPropDigits>3</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.634</nVarValue> <nVarDigits>3</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>.241</nPropValue> <nPropDigits>3</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.935</nVarValue> <nVarDigits>3</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>0</nPropValue> <nPropDigits>0</nPropDigits> </PropertyValue> </NumValues> </PureOrMixtureData> <PureOrMixtureData> <Component> <RegNum> <nOrgNum>6</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>RDC</sCompiler> <sContributor>TRC</sContributor> <dateDateAdded>8/7/2003</dateDateAdded> <Property> <nPropNumber>1</nPropNumber> <Property-MethodID> <PropertyGroup> <CompositionAtPhaseEquilibrium> <ePropName>Mole fraction</ePropName> <eMethodName>Other</eMethodName> </CompositionAtPhaseEquilibrium> </PropertyGroup> <RegNum> <nOrgNum>6</nOrgNum> </RegNum> </Property-MethodID> <PropPhaseID> <ePropPhase>Liquid mixture 1</ePropPhase> </PropPhaseID> <ePresentation>Direct value, X</ePresentation> </Property> <Property> <nPropNumber>2</nPropNumber> <Property-MethodID> <PropertyGroup> <CompositionAtPhaseEquilibrium> <ePropName>Mole fraction</ePropName> <eMethodName>Other</eMethodName> </CompositionAtPhaseEquilibrium> </PropertyGroup> <RegNum> <nOrgNum>1</nOrgNum> </RegNum> </Property-MethodID> <PropPhaseID> <ePropPhase>Liquid mixture 2</ePropPhase> </PropPhaseID> <ePresentation>Direct value, X</ePresentation> </Property> <Property> <nPropNumber>3</nPropNumber> <Property-MethodID> <PropertyGroup> <CompositionAtPhaseEquilibrium> <ePropName>Mole fraction</ePropName> <eMethodName>Other</eMethodName> </CompositionAtPhaseEquilibrium> </PropertyGroup> <RegNum> <nOrgNum>6</nOrgNum> </RegNum> </Property-MethodID> <PropPhaseID> <ePropPhase>Liquid mixture 2</ePropPhase> </PropPhaseID> <ePresentation>Direct value, X</ePresentation> </Property> <PhaseID> <ePhase>Liquid mixture 1</ePhase> </PhaseID> <PhaseID> <ePhase>Liquid mixture 2</ePhase> </PhaseID> <Constraint> <ConstraintID> <ConstraintType> <ePressure>Pressure, kPa</ePressure> </ConstraintType> </ConstraintID> <nConstraintValue>101.3</nConstraintValue> <nConstrDigits>4</nConstrDigits> </Constraint> <Constraint> <ConstraintID> <ConstraintType> <eTemperature>Temperature, K</eTemperature> </ConstraintType> </ConstraintID> <nConstraintValue>298.2</nConstraintValue> <nConstrDigits>4</nConstrDigits> </Constraint> <Variable> <nVarNumber>1</nVarNumber> <VariableID> <VariableType> <eComponentComposition>Mole fraction</eComponentComposition> </VariableType> <RegNum> <nOrgNum>1</nOrgNum> </RegNum> </VariableID> <VarPhaseID> <eVarPhase>Liquid mixture 1</eVarPhase> </VarPhaseID> </Variable> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.493</nVarValue> <nVarDigits>3</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>.371</nPropValue> <nPropDigits>3</nPropDigits> </PropertyValue> <PropertyValue> <nPropNumber>2</nPropNumber> <nPropValue>.007</nPropValue> <nPropDigits>1</nPropDigits> </PropertyValue> <PropertyValue> <nPropNumber>3</nPropNumber> <nPropValue>.007</nPropValue> <nPropDigits>1</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.36</nVarValue> <nVarDigits>3</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>.489</nPropValue> <nPropDigits>3</nPropDigits> </PropertyValue> <PropertyValue> <nPropNumber>2</nPropNumber> <nPropValue>.007</nPropValue> <nPropDigits>1</nPropDigits> </PropertyValue> <PropertyValue> <nPropNumber>3</nPropNumber> <nPropValue>.007</nPropValue> <nPropDigits>1</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.264</nVarValue> <nVarDigits>3</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>.574</nPropValue> <nPropDigits>3</nPropDigits> </PropertyValue> <PropertyValue> <nPropNumber>2</nPropNumber> <nPropValue>.007</nPropValue> <nPropDigits>1</nPropDigits> </PropertyValue> <PropertyValue> <nPropNumber>3</nPropNumber> <nPropValue>.007</nPropValue> <nPropDigits>1</nPropDigits> </PropertyValue> </NumValues> </PureOrMixtureData> </DataReport>