ThermoML Data file

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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>mon</sAuthor1> <sAuthor2>woo</sAuthor2> <nAuthorn>1</nAuthorn> </TRCRefID> <eType>journal</eType> <eSourceType>Original</eSourceType> <sAuthor>Monarrez, C.[Cassandra]</sAuthor> <sAuthor>Woo, J. H.[Jee H.]</sAuthor> <sAuthor>Taylor, P. G.[Priscilla G.]</sAuthor> <sAuthor>Tran, A. M.[Anh M.]</sAuthor> <sAuthor>Acree Jr., W. E.[William E.]</sAuthor> <sPubName>J. Chem. Eng. Data</sPubName> <yrPubYr>2003</yrPubYr> <dateCit>2003-07-01</dateCit> <sTitle>Solubility in Binary Solvent Mixtures: Pyrene Dissolved in Alcohol + Acetonitrile Mixtures at 299.2 K</sTitle> <sAbstract>Experimental solubilities are reported for pyrene dissolved in seven binary alcohol + acetonitrile solvent mixtures at 26 C. The alcohol cosolvents studied were 1-propanol, 2-propanol, 1-butanol, 2-butanol, 2-methyl-1-propanol, 3-methyl-1-butanol and 2-pentanol. 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 seven systems tudied, the Combined NIBS/Redlich-Kister equation was found to mathematically describe the experimental solubility data to within an overall average absolute deviation of approximately 1.0 %.</sAbstract> <sKeyword>pyrene solubilities</sKeyword> <sKeyword>binary solvents</sKeyword> <sKeyword>alcohol cosolvents</sKeyword> <sKeyword>acetonitrile cosolvent</sKeyword> <sVol>48</sVol> <sPage>736-738</sPage> </Citation> <Compound> <RegNum> <nOrgNum>1</nOrgNum> </RegNum> <sCommonName>pyrene</sCommonName> <sFormulaMolec>C16H10</sFormulaMolec> <Sample> <nSampleNm>1</nSampleNm> <eSource>Commercial source</eSource> <purity> <nStep>1</nStep> <nPurityMol>98</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> 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</VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>.00748</nPropValue> <nPropDigits>3</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>1</nVarValue> <nVarDigits>5</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>.00614</nPropValue> <nPropDigits>3</nPropDigits> </PropertyValue> </NumValues> </PureOrMixtureData> <PureOrMixtureData> <Component> <RegNum> <nOrgNum>9</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>2/21/2003</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> <RegNum> <nOrgNum>1</nOrgNum> </RegNum> </PhaseID> <Constraint> <ConstraintID> <ConstraintType> <eTemperature>Temperature, K</eTemperature> </ConstraintType> </ConstraintID> <nConstraintValue>299.2</nConstraintValue> <nConstrDigits>4</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>9</nOrgNum> </RegNum> </VariableID> <VarPhaseID> <eVarPhase>Liquid</eVarPhase> </VarPhaseID> <Solvent> <RegNum> <nOrgNum>9</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>.00439</nPropValue> <nPropDigits>3</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.1711</nVarValue> <nVarDigits>4</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>.00839</nPropValue> <nPropDigits>3</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.3252</nVarValue> <nVarDigits>4</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>.01118</nPropValue> <nPropDigits>4</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.5339</nVarValue> <nVarDigits>4</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>.01225</nPropValue> <nPropDigits>4</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.6346</nVarValue> <nVarDigits>4</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>.01163</nPropValue> <nPropDigits>4</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.73</nVarValue> <nVarDigits>4</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>.0105</nPropValue> <nPropDigits>4</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.8762</nVarValue> <nVarDigits>4</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>.00807</nPropValue> <nPropDigits>3</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.9412</nVarValue> <nVarDigits>4</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>.00693</nPropValue> <nPropDigits>3</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>1</nVarValue> <nVarDigits>5</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>.00614</nPropValue> <nPropDigits>3</nPropDigits> </PropertyValue> </NumValues> </PureOrMixtureData> <PureOrMixtureData> <Component> <RegNum> <nOrgNum>9</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>2/21/2003</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> <RegNum> <nOrgNum>1</nOrgNum> </RegNum> </PhaseID> <Constraint> <ConstraintID> <ConstraintType> <eTemperature>Temperature, K</eTemperature> </ConstraintType> </ConstraintID> <nConstraintValue>299.2</nConstraintValue> <nConstrDigits>4</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>9</nOrgNum> </RegNum> </VariableID> <VarPhaseID> <eVarPhase>Liquid</eVarPhase> </VarPhaseID> <Solvent> <RegNum> <nOrgNum>9</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>.00326</nPropValue> <nPropDigits>3</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.1714</nVarValue> <nVarDigits>4</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>.00642</nPropValue> <nPropDigits>3</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.3074</nVarValue> <nVarDigits>4</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>.00872</nPropValue> <nPropDigits>3</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.5382</nVarValue> <nVarDigits>4</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>.01072</nPropValue> <nPropDigits>4</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.6341</nVarValue> <nVarDigits>4</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>.01058</nPropValue> <nPropDigits>4</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.7241</nVarValue> <nVarDigits>4</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>.00992</nPropValue> <nPropDigits>3</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.8686</nVarValue> <nVarDigits>4</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>.00802</nPropValue> <nPropDigits>3</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.9331</nVarValue> <nVarDigits>4</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>.00699</nPropValue> <nPropDigits>3</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>1</nVarValue> <nVarDigits>5</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>.00614</nPropValue> <nPropDigits>3</nPropDigits> </PropertyValue> </NumValues> </PureOrMixtureData> <PureOrMixtureData> <Component> <RegNum> <nOrgNum>9</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>2/21/2003</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> <RegNum> <nOrgNum>1</nOrgNum> </RegNum> </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>299.2</nConstraintValue> <nConstrDigits>4</nConstrDigits> </Constraint> <Variable> <nVarNumber>1</nVarNumber> <VariableID> <VariableType> <eSolventComposition>Solvent: Mole fraction</eSolventComposition> </VariableType> <RegNum> <nOrgNum>9</nOrgNum> </RegNum> </VariableID> <VarPhaseID> <eVarPhase>Liquid</eVarPhase> </VarPhaseID> <Solvent> <RegNum> <nOrgNum>9</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>.00546</nPropValue> <nPropDigits>3</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.1981</nVarValue> <nVarDigits>4</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>.00995</nPropValue> <nPropDigits>3</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.3709</nVarValue> <nVarDigits>4</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>.01223</nPropValue> <nPropDigits>4</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.5829</nVarValue> <nVarDigits>4</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>.01296</nPropValue> <nPropDigits>4</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.66</nVarValue> <nVarDigits>4</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>.01255</nPropValue> <nPropDigits>4</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.7605</nVarValue> <nVarDigits>4</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>.01132</nPropValue> <nPropDigits>4</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.8929</nVarValue> <nVarDigits>4</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>.00849</nPropValue> <nPropDigits>3</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.9461</nVarValue> <nVarDigits>4</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>.00734</nPropValue> <nPropDigits>3</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>1</nVarValue> <nVarDigits>5</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>.00614</nPropValue> <nPropDigits>3</nPropDigits> </PropertyValue> </NumValues> </PureOrMixtureData> <PureOrMixtureData> <Component> <RegNum> <nOrgNum>9</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>2/21/2003</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> <RegNum> <nOrgNum>1</nOrgNum> </RegNum> </PhaseID> <Constraint> <ConstraintID> <ConstraintType> <eTemperature>Temperature, K</eTemperature> </ConstraintType> </ConstraintID> <nConstraintValue>299.2</nConstraintValue> <nConstrDigits>4</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>9</nOrgNum> </RegNum> </VariableID> <VarPhaseID> <eVarPhase>Liquid</eVarPhase> </VarPhaseID> <Solvent> <RegNum> <nOrgNum>9</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>.0064</nPropValue> <nPropDigits>3</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.2222</nVarValue> <nVarDigits>4</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>.01274</nPropValue> <nPropDigits>4</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.3733</nVarValue> <nVarDigits>4</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>.01517</nPropValue> <nPropDigits>4</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.569</nVarValue> <nVarDigits>4</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>.01584</nPropValue> <nPropDigits>4</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.6652</nVarValue> <nVarDigits>4</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>.01495</nPropValue> <nPropDigits>4</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.7626</nVarValue> <nVarDigits>4</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>.01283</nPropValue> <nPropDigits>4</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.89</nVarValue> <nVarDigits>4</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>.00925</nPropValue> <nPropDigits>3</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.9494</nVarValue> <nVarDigits>4</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>.00751</nPropValue> <nPropDigits>3</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>1</nVarValue> <nVarDigits>5</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>.00614</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>VVD</sCompiler> <sContributor>TRC</sContributor> <dateDateAdded>7/1/2003</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> <RegNum> <nOrgNum>1</nOrgNum> </RegNum> </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>299.2</nVarValue> <nVarDigits>4</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>.00426</nPropValue> <nPropDigits>3</nPropDigits> </PropertyValue> </NumValues> </PureOrMixtureData> <PureOrMixtureData> <Component> <RegNum> <nOrgNum>9</nOrgNum> </RegNum> <nSampleNm>1</nSampleNm> </Component> <Component> <RegNum> <nOrgNum>1</nOrgNum> </RegNum> <nSampleNm>1</nSampleNm> </Component> <eExpPurpose>Principal objective of the work</eExpPurpose> <sCompiler>VVD</sCompiler> <sContributor>TRC</sContributor> <dateDateAdded>7/1/2003</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> <RegNum> <nOrgNum>1</nOrgNum> </RegNum> </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>299.2</nVarValue> <nVarDigits>4</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>.00614</nPropValue> <nPropDigits>3</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>VVD</sCompiler> <sContributor>TRC</sContributor> <dateDateAdded>7/1/2003</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> <RegNum> <nOrgNum>1</nOrgNum> </RegNum> </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>299.2</nVarValue> <nVarDigits>4</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>.0029</nPropValue> <nPropDigits>3</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>VVD</sCompiler> <sContributor>TRC</sContributor> <dateDateAdded>7/1/2003</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> <RegNum> <nOrgNum>1</nOrgNum> </RegNum> </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>299.2</nVarValue> <nVarDigits>4</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>.00622</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>VVD</sCompiler> <sContributor>TRC</sContributor> <dateDateAdded>7/1/2003</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> <RegNum> <nOrgNum>1</nOrgNum> </RegNum> </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>299.2</nVarValue> <nVarDigits>4</nVarDigits> </VariableValue> <VariableValue> <nVarNumber>2</nVarNumber> <nVarValue>101</nVarValue> <nVarDigits>3</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>.00439</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>VVD</sCompiler> <sContributor>TRC</sContributor> <dateDateAdded>7/1/2003</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> <RegNum> <nOrgNum>1</nOrgNum> </RegNum> </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>299.2</nVarValue> <nVarDigits>4</nVarDigits> </VariableValue> <VariableValue> <nVarNumber>2</nVarNumber> <nVarValue>101</nVarValue> <nVarDigits>3</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>.00326</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>VVD</sCompiler> <sContributor>TRC</sContributor> <dateDateAdded>7/1/2003</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> <RegNum> <nOrgNum>1</nOrgNum> </RegNum> </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>299.2</nVarValue> <nVarDigits>4</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>.00546</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>VVD</sCompiler> <sContributor>TRC</sContributor> <dateDateAdded>7/1/2003</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> <RegNum> <nOrgNum>1</nOrgNum> </RegNum> </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>299.2</nVarValue> <nVarDigits>4</nVarDigits> </VariableValue> <VariableValue> <nVarNumber>2</nVarNumber> <nVarValue>101</nVarValue> <nVarDigits>3</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>.0064</nPropValue> <nPropDigits>3</nPropDigits> </PropertyValue> </NumValues> </PureOrMixtureData> </DataReport>