ThermoML Data file

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<?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>2004</yrYrPub> <sAuthor1>liu</sAuthor1> <sAuthor2>chi</sAuthor2> <nAuthorn>0</nAuthorn> </TRCRefID> <eType>journal</eType> <eSourceType>Original</eSourceType> <sAuthor>Liu, J.-f.[Jing-fu]</sAuthor> <sAuthor>Chi, Y.-g.[Yu-guang]</sAuthor> <sAuthor>Peng, J.-f.[Jin-feng]</sAuthor> <sAuthor>Jiang, G.-b.[Gui-bin]</sAuthor> <sAuthor>Jonsson, J. A.[Jan Ake]</sAuthor> <sPubName>J. Chem. Eng. Data</sPubName> <yrPubYr>2004</yrPubYr> <dateCit>2004-10-29</dateCit> <sTitle>Ionic Liquids/Water Distribution Ratios of Some Polycyclic Aromatic Hydrocarbons</sTitle> <sAbstract>By using the shake-flask procedure, the distribution ratios (D) at infinite dilution and 298.1 K of 15 polycyclic aromatic hydrocarbons (PAHs) between room-temperature ionic liquids, 1-alkyl-3-methylimiazolium hexafluorophosphates ([CnMIM][PF6], n ) 4 and 8), and water were determined. The log D values are in the range of 3.34-4.36, which increased very slowly with the molar mass of PAHs.</sAbstract> <sKeyword>ionic liquids</sKeyword> <sKeyword>distribution ratios</sKeyword> <sKeyword>polycyclic aromatic hydrocarbons</sKeyword> <sVol>49</sVol> <sPage>1422-1424</sPage> </Citation> <Compound> <RegNum> <nOrgNum>1</nOrgNum> </RegNum> <sCommonName>naphthalene</sCommonName> <sFormulaMolec>C10H8</sFormulaMolec> <Sample> <nSampleNm>1</nSampleNm> <eSource>Commercial source</eSource> </Sample> </Compound> <Compound> <RegNum> <nOrgNum>2</nOrgNum> </RegNum> <sCommonName>acenaphthene</sCommonName> <sFormulaMolec>C12H10</sFormulaMolec> <Sample> <nSampleNm>1</nSampleNm> <eSource>Commercial source</eSource> </Sample> </Compound> <Compound> <RegNum> <nOrgNum>3</nOrgNum> </RegNum> <sCommonName>fluorene</sCommonName> <sFormulaMolec>C13H10</sFormulaMolec> <Sample> <nSampleNm>1</nSampleNm> <eSource>Commercial source</eSource> </Sample> </Compound> <Compound> <RegNum> <nOrgNum>4</nOrgNum> 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<Compound> <RegNum> <nOrgNum>13</nOrgNum> </RegNum> <sCommonName>dibenz[a,h]anthracene</sCommonName> <sFormulaMolec>C22H14</sFormulaMolec> <Sample> <nSampleNm>1</nSampleNm> <eSource>Commercial source</eSource> </Sample> </Compound> <Compound> <RegNum> <nOrgNum>14</nOrgNum> </RegNum> <sCommonName>benzo[ghi]perylene</sCommonName> <sFormulaMolec>C22H12</sFormulaMolec> <Sample> <nSampleNm>1</nSampleNm> <eSource>Commercial source</eSource> </Sample> </Compound> <Compound> <RegNum> <nOrgNum>15</nOrgNum> </RegNum> <sCommonName>water</sCommonName> <sFormulaMolec>H2O</sFormulaMolec> <Sample> <nSampleNm>1</nSampleNm> <eSource>Commercial source</eSource> </Sample> </Compound> <Compound> <RegNum> <nOrgNum>16</nOrgNum> </RegNum> <sCommonName>1-butyl-3-methylimidazolium hexaflourophosphate</sCommonName> <sFormulaMolec>C8H15F6N2P</sFormulaMolec> <Sample> <nSampleNm>1</nSampleNm> <eSource>Commercial source</eSource> </Sample> </Compound> <Compound> <RegNum> <nOrgNum>17</nOrgNum> </RegNum> 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</VariableID> </Variable> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>298.1</nVarValue> <nVarDigits>4</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>15849</nPropValue> <nPropDigits>5</nPropDigits> <PropUncertainty> <nUncertAssessNum>1</nUncertAssessNum> <nExpandUncertValue>5531</nExpandUncertValue> </PropUncertainty> </PropertyValue> </NumValues> </PureOrMixtureData> <PureOrMixtureData> <Component> <RegNum> <nOrgNum>7</nOrgNum> </RegNum> <nSampleNm>1</nSampleNm> </Component> <Component> <RegNum> <nOrgNum>15</nOrgNum> </RegNum> <nSampleNm>1</nSampleNm> </Component> <Component> <RegNum> <nOrgNum>16</nOrgNum> </RegNum> <nSampleNm>1</nSampleNm> </Component> <eExpPurpose>Principal objective of the work</eExpPurpose> <sCompiler>CDG</sCompiler> <sContributor>TRC</sContributor> <dateDateAdded>10/20/2004</dateDateAdded> <Property> <nPropNumber>1</nPropNumber> <Property-MethodID> <PropertyGroup> <CompositionAtPhaseEquilibrium> <ePropName>Mass concentration, kg/m3</ePropName> <eMethodName>Chromatography</eMethodName> </CompositionAtPhaseEquilibrium> </PropertyGroup> <RegNum> <nOrgNum>7</nOrgNum> </RegNum> </Property-MethodID> <PropPhaseID> <ePropPhase>Liquid mixture 1</ePropPhase> </PropPhaseID> <ePresentation>Ratio with the reference state, X/X(REF)</ePresentation> <eRefStateType>Phase in equilibrium with primary phase at the same temperature and pressure</eRefStateType> <RefPhaseID> <eRefPhase>Liquid</eRefPhase> </RefPhaseID> <PropUncertainty> <nUncertAssessNum>1</nUncertAssessNum> <sUncertEvaluator>Author</sUncertEvaluator> <nUncertLevOfConfid>95</nUncertLevOfConfid> </PropUncertainty> </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> <eComponentComposition>Mole fraction</eComponentComposition> </ConstraintType> <RegNum> <nOrgNum>7</nOrgNum> </RegNum> </ConstraintID> <ConstraintPhaseID> <eConstraintPhase>Liquid mixture 2</eConstraintPhase> </ConstraintPhaseID> <nConstraintValue>0</nConstraintValue> <nConstrDigits>0</nConstrDigits> </Constraint> <Variable> <nVarNumber>1</nVarNumber> <VariableID> <VariableType> <eTemperature>Temperature, K</eTemperature> </VariableType> </VariableID> </Variable> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>298.1</nVarValue> <nVarDigits>4</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>16218</nPropValue> <nPropDigits>5</nPropDigits> <PropUncertainty> <nUncertAssessNum>1</nUncertAssessNum> <nExpandUncertValue>4675</nExpandUncertValue> </PropUncertainty> </PropertyValue> </NumValues> </PureOrMixtureData> <PureOrMixtureData> <Component> <RegNum> <nOrgNum>8</nOrgNum> </RegNum> <nSampleNm>1</nSampleNm> </Component> <Component> <RegNum> <nOrgNum>15</nOrgNum> </RegNum> <nSampleNm>1</nSampleNm> </Component> <Component> <RegNum> <nOrgNum>16</nOrgNum> </RegNum> <nSampleNm>1</nSampleNm> </Component> <eExpPurpose>Principal objective of the work</eExpPurpose> <sCompiler>CDG</sCompiler> <sContributor>TRC</sContributor> <dateDateAdded>10/20/2004</dateDateAdded> <Property> <nPropNumber>1</nPropNumber> <Property-MethodID> <PropertyGroup> <CompositionAtPhaseEquilibrium> <ePropName>Mass concentration, kg/m3</ePropName> <eMethodName>Chromatography</eMethodName> </CompositionAtPhaseEquilibrium> </PropertyGroup> <RegNum> <nOrgNum>8</nOrgNum> </RegNum> </Property-MethodID> <PropPhaseID> <ePropPhase>Liquid mixture 1</ePropPhase> </PropPhaseID> <ePresentation>Ratio with the reference state, X/X(REF)</ePresentation> <eRefStateType>Phase in equilibrium with primary phase at the same temperature and pressure</eRefStateType> <RefPhaseID> <eRefPhase>Liquid</eRefPhase> </RefPhaseID> <PropUncertainty> <nUncertAssessNum>1</nUncertAssessNum> <sUncertEvaluator>Author</sUncertEvaluator> <nUncertLevOfConfid>95</nUncertLevOfConfid> </PropUncertainty> </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> <eComponentComposition>Mole fraction</eComponentComposition> </ConstraintType> <RegNum> <nOrgNum>8</nOrgNum> </RegNum> </ConstraintID> <ConstraintPhaseID> <eConstraintPhase>Liquid mixture 2</eConstraintPhase> </ConstraintPhaseID> <nConstraintValue>0</nConstraintValue> <nConstrDigits>0</nConstrDigits> </Constraint> <Variable> <nVarNumber>1</nVarNumber> <VariableID> <VariableType> <eTemperature>Temperature, K</eTemperature> </VariableType> </VariableID> </Variable> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>298.1</nVarValue> <nVarDigits>4</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>16596</nPropValue> <nPropDigits>5</nPropDigits> <PropUncertainty> <nUncertAssessNum>1</nUncertAssessNum> <nExpandUncertValue>6846</nExpandUncertValue> </PropUncertainty> </PropertyValue> </NumValues> </PureOrMixtureData> <PureOrMixtureData> <Component> <RegNum> <nOrgNum>9</nOrgNum> </RegNum> <nSampleNm>1</nSampleNm> </Component> <Component> <RegNum> <nOrgNum>15</nOrgNum> </RegNum> <nSampleNm>1</nSampleNm> </Component> <Component> <RegNum> <nOrgNum>16</nOrgNum> </RegNum> <nSampleNm>1</nSampleNm> </Component> <eExpPurpose>Principal objective of the work</eExpPurpose> <sCompiler>CDG</sCompiler> <sContributor>TRC</sContributor> <dateDateAdded>10/20/2004</dateDateAdded> <Property> <nPropNumber>1</nPropNumber> <Property-MethodID> <PropertyGroup> <CompositionAtPhaseEquilibrium> <ePropName>Mass concentration, kg/m3</ePropName> <eMethodName>Chromatography</eMethodName> </CompositionAtPhaseEquilibrium> </PropertyGroup> <RegNum> <nOrgNum>9</nOrgNum> </RegNum> </Property-MethodID> <PropPhaseID> <ePropPhase>Liquid mixture 1</ePropPhase> </PropPhaseID> <ePresentation>Ratio with the reference state, X/X(REF)</ePresentation> <eRefStateType>Phase in equilibrium with primary phase at the same temperature and pressure</eRefStateType> <RefPhaseID> <eRefPhase>Liquid</eRefPhase> </RefPhaseID> <PropUncertainty> <nUncertAssessNum>1</nUncertAssessNum> <sUncertEvaluator>Author</sUncertEvaluator> <nUncertLevOfConfid>95</nUncertLevOfConfid> </PropUncertainty> </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> <eComponentComposition>Mole fraction</eComponentComposition> </ConstraintType> <RegNum> <nOrgNum>9</nOrgNum> </RegNum> </ConstraintID> <ConstraintPhaseID> <eConstraintPhase>Liquid mixture 2</eConstraintPhase> </ConstraintPhaseID> <nConstraintValue>0</nConstraintValue> <nConstrDigits>0</nConstrDigits> </Constraint> <Variable> <nVarNumber>1</nVarNumber> <VariableID> <VariableType> <eTemperature>Temperature, K</eTemperature> </VariableType> </VariableID> </Variable> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>298.1</nVarValue> <nVarDigits>4</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>16596</nPropValue> <nPropDigits>5</nPropDigits> <PropUncertainty> <nUncertAssessNum>1</nUncertAssessNum> <nExpandUncertValue>6313</nExpandUncertValue> </PropUncertainty> </PropertyValue> </NumValues> </PureOrMixtureData> <PureOrMixtureData> <Component> <RegNum> <nOrgNum>10</nOrgNum> </RegNum> <nSampleNm>1</nSampleNm> </Component> <Component> <RegNum> <nOrgNum>15</nOrgNum> </RegNum> <nSampleNm>1</nSampleNm> </Component> <Component> <RegNum> <nOrgNum>16</nOrgNum> </RegNum> <nSampleNm>1</nSampleNm> </Component> <eExpPurpose>Principal objective of the work</eExpPurpose> <sCompiler>CDG</sCompiler> <sContributor>TRC</sContributor> <dateDateAdded>10/20/2004</dateDateAdded> <Property> <nPropNumber>1</nPropNumber> <Property-MethodID> <PropertyGroup> <CompositionAtPhaseEquilibrium> <ePropName>Mass concentration, kg/m3</ePropName> <eMethodName>Chromatography</eMethodName> </CompositionAtPhaseEquilibrium> </PropertyGroup> <RegNum> <nOrgNum>10</nOrgNum> </RegNum> </Property-MethodID> <PropPhaseID> <ePropPhase>Liquid mixture 1</ePropPhase> </PropPhaseID> <ePresentation>Ratio with the reference state, X/X(REF)</ePresentation> <eRefStateType>Phase in equilibrium with primary phase at the same temperature and pressure</eRefStateType> <RefPhaseID> <eRefPhase>Liquid</eRefPhase> </RefPhaseID> <PropUncertainty> <nUncertAssessNum>1</nUncertAssessNum> <sUncertEvaluator>Author</sUncertEvaluator> <nUncertLevOfConfid>95</nUncertLevOfConfid> </PropUncertainty> </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> <eComponentComposition>Mole fraction</eComponentComposition> </ConstraintType> <RegNum> <nOrgNum>10</nOrgNum> </RegNum> </ConstraintID> <ConstraintPhaseID> <eConstraintPhase>Liquid mixture 2</eConstraintPhase> </ConstraintPhaseID> <nConstraintValue>0</nConstraintValue> <nConstrDigits>0</nConstrDigits> </Constraint> <Variable> <nVarNumber>1</nVarNumber> <VariableID> <VariableType> <eTemperature>Temperature, K</eTemperature> </VariableType> </VariableID> </Variable> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>298.1</nVarValue> <nVarDigits>4</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>20417</nPropValue> <nPropDigits>5</nPropDigits> <PropUncertainty> <nUncertAssessNum>1</nUncertAssessNum> <nExpandUncertValue>9782</nExpandUncertValue> </PropUncertainty> </PropertyValue> </NumValues> </PureOrMixtureData> <PureOrMixtureData> <Component> <RegNum> <nOrgNum>11</nOrgNum> </RegNum> <nSampleNm>1</nSampleNm> </Component> <Component> <RegNum> <nOrgNum>15</nOrgNum> </RegNum> <nSampleNm>1</nSampleNm> </Component> <Component> <RegNum> <nOrgNum>16</nOrgNum> </RegNum> <nSampleNm>1</nSampleNm> </Component> <eExpPurpose>Principal objective of the work</eExpPurpose> <sCompiler>CDG</sCompiler> <sContributor>TRC</sContributor> <dateDateAdded>10/20/2004</dateDateAdded> <Property> <nPropNumber>1</nPropNumber> <Property-MethodID> <PropertyGroup> <CompositionAtPhaseEquilibrium> <ePropName>Mass concentration, kg/m3</ePropName> <eMethodName>Chromatography</eMethodName> </CompositionAtPhaseEquilibrium> </PropertyGroup> <RegNum> <nOrgNum>11</nOrgNum> </RegNum> </Property-MethodID> <PropPhaseID> <ePropPhase>Liquid mixture 1</ePropPhase> </PropPhaseID> <ePresentation>Ratio with the reference state, X/X(REF)</ePresentation> <eRefStateType>Phase in equilibrium with primary phase at the same temperature and pressure</eRefStateType> <RefPhaseID> <eRefPhase>Liquid</eRefPhase> </RefPhaseID> <PropUncertainty> <nUncertAssessNum>1</nUncertAssessNum> <sUncertEvaluator>Author</sUncertEvaluator> <nUncertLevOfConfid>95</nUncertLevOfConfid> </PropUncertainty> </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> <eComponentComposition>Mole fraction</eComponentComposition> </ConstraintType> <RegNum> <nOrgNum>11</nOrgNum> </RegNum> </ConstraintID> <ConstraintPhaseID> <eConstraintPhase>Liquid mixture 2</eConstraintPhase> </ConstraintPhaseID> <nConstraintValue>0</nConstraintValue> <nConstrDigits>0</nConstrDigits> </Constraint> <Variable> <nVarNumber>1</nVarNumber> <VariableID> <VariableType> <eTemperature>Temperature, K</eTemperature> </VariableType> </VariableID> </Variable> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>298.1</nVarValue> <nVarDigits>4</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>19953</nPropValue> <nPropDigits>5</nPropDigits> <PropUncertainty> <nUncertAssessNum>1</nUncertAssessNum> <nExpandUncertValue>11670</nExpandUncertValue> </PropUncertainty> </PropertyValue> </NumValues> </PureOrMixtureData> <PureOrMixtureData> <Component> <RegNum> <nOrgNum>12</nOrgNum> </RegNum> <nSampleNm>1</nSampleNm> </Component> <Component> <RegNum> <nOrgNum>15</nOrgNum> </RegNum> <nSampleNm>1</nSampleNm> </Component> <Component> <RegNum> <nOrgNum>16</nOrgNum> </RegNum> <nSampleNm>1</nSampleNm> </Component> <eExpPurpose>Principal objective of the work</eExpPurpose> <sCompiler>CDG</sCompiler> <sContributor>TRC</sContributor> <dateDateAdded>10/20/2004</dateDateAdded> <Property> <nPropNumber>1</nPropNumber> <Property-MethodID> <PropertyGroup> <CompositionAtPhaseEquilibrium> <ePropName>Mass concentration, kg/m3</ePropName> <eMethodName>Chromatography</eMethodName> </CompositionAtPhaseEquilibrium> </PropertyGroup> <RegNum> <nOrgNum>12</nOrgNum> </RegNum> </Property-MethodID> <PropPhaseID> <ePropPhase>Liquid mixture 1</ePropPhase> </PropPhaseID> <ePresentation>Ratio with the reference state, X/X(REF)</ePresentation> <eRefStateType>Phase in equilibrium with primary phase at the same temperature and pressure</eRefStateType> <RefPhaseID> <eRefPhase>Liquid</eRefPhase> </RefPhaseID> <PropUncertainty> <nUncertAssessNum>1</nUncertAssessNum> <sUncertEvaluator>Author</sUncertEvaluator> <nUncertLevOfConfid>95</nUncertLevOfConfid> </PropUncertainty> </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> <eComponentComposition>Mole fraction</eComponentComposition> </ConstraintType> <RegNum> <nOrgNum>12</nOrgNum> </RegNum> </ConstraintID> <ConstraintPhaseID> <eConstraintPhase>Liquid mixture 2</eConstraintPhase> </ConstraintPhaseID> <nConstraintValue>0</nConstraintValue> <nConstrDigits>0</nConstrDigits> </Constraint> <Variable> <nVarNumber>1</nVarNumber> <VariableID> <VariableType> <eTemperature>Temperature, K</eTemperature> </VariableType> </VariableID> </Variable> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>298.1</nVarValue> <nVarDigits>4</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>20893</nPropValue> <nPropDigits>5</nPropDigits> <PropUncertainty> <nUncertAssessNum>1</nUncertAssessNum> <nExpandUncertValue>10730</nExpandUncertValue> </PropUncertainty> </PropertyValue> </NumValues> </PureOrMixtureData> <PureOrMixtureData> <Component> <RegNum> <nOrgNum>13</nOrgNum> </RegNum> <nSampleNm>1</nSampleNm> </Component> <Component> <RegNum> <nOrgNum>15</nOrgNum> </RegNum> <nSampleNm>1</nSampleNm> </Component> <Component> <RegNum> <nOrgNum>16</nOrgNum> </RegNum> <nSampleNm>1</nSampleNm> </Component> <eExpPurpose>Principal objective of the work</eExpPurpose> <sCompiler>CDG</sCompiler> <sContributor>TRC</sContributor> <dateDateAdded>10/20/2004</dateDateAdded> <Property> <nPropNumber>1</nPropNumber> <Property-MethodID> <PropertyGroup> <CompositionAtPhaseEquilibrium> <ePropName>Mass concentration, kg/m3</ePropName> <eMethodName>Chromatography</eMethodName> </CompositionAtPhaseEquilibrium> </PropertyGroup> <RegNum> <nOrgNum>13</nOrgNum> </RegNum> </Property-MethodID> <PropPhaseID> <ePropPhase>Liquid mixture 1</ePropPhase> </PropPhaseID> <ePresentation>Ratio with the reference state, X/X(REF)</ePresentation> <eRefStateType>Phase in equilibrium with primary phase at the same temperature and pressure</eRefStateType> <RefPhaseID> <eRefPhase>Liquid</eRefPhase> </RefPhaseID> <PropUncertainty> <nUncertAssessNum>1</nUncertAssessNum> <sUncertEvaluator>Author</sUncertEvaluator> <nUncertLevOfConfid>95</nUncertLevOfConfid> </PropUncertainty> </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> <eComponentComposition>Mole fraction</eComponentComposition> </ConstraintType> <RegNum> <nOrgNum>13</nOrgNum> </RegNum> </ConstraintID> <ConstraintPhaseID> <eConstraintPhase>Liquid mixture 2</eConstraintPhase> </ConstraintPhaseID> <nConstraintValue>0</nConstraintValue> <nConstrDigits>0</nConstrDigits> </Constraint> <Variable> <nVarNumber>1</nVarNumber> <VariableID> <VariableType> <eTemperature>Temperature, K</eTemperature> </VariableType> </VariableID> </Variable> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>298.1</nVarValue> <nVarDigits>4</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>19953</nPropValue> <nPropDigits>5</nPropDigits> <PropUncertainty> <nUncertAssessNum>1</nUncertAssessNum> <nExpandUncertValue>12407</nExpandUncertValue> </PropUncertainty> </PropertyValue> </NumValues> </PureOrMixtureData> <PureOrMixtureData> <Component> <RegNum> <nOrgNum>14</nOrgNum> </RegNum> <nSampleNm>1</nSampleNm> </Component> <Component> <RegNum> <nOrgNum>15</nOrgNum> </RegNum> <nSampleNm>1</nSampleNm> </Component> <Component> <RegNum> <nOrgNum>16</nOrgNum> </RegNum> <nSampleNm>1</nSampleNm> </Component> <eExpPurpose>Principal objective of the work</eExpPurpose> <sCompiler>CDG</sCompiler> <sContributor>TRC</sContributor> <dateDateAdded>10/20/2004</dateDateAdded> <Property> <nPropNumber>1</nPropNumber> <Property-MethodID> <PropertyGroup> <CompositionAtPhaseEquilibrium> <ePropName>Mass concentration, kg/m3</ePropName> <eMethodName>Chromatography</eMethodName> </CompositionAtPhaseEquilibrium> </PropertyGroup> <RegNum> <nOrgNum>14</nOrgNum> </RegNum> </Property-MethodID> <PropPhaseID> <ePropPhase>Liquid mixture 1</ePropPhase> </PropPhaseID> <ePresentation>Ratio with the reference state, X/X(REF)</ePresentation> <eRefStateType>Phase in equilibrium with primary phase at the same temperature and pressure</eRefStateType> <RefPhaseID> <eRefPhase>Liquid</eRefPhase> </RefPhaseID> <PropUncertainty> <nUncertAssessNum>1</nUncertAssessNum> <sUncertEvaluator>Author</sUncertEvaluator> <nUncertLevOfConfid>95</nUncertLevOfConfid> </PropUncertainty> </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> <eComponentComposition>Mole fraction</eComponentComposition> </ConstraintType> <RegNum> <nOrgNum>14</nOrgNum> </RegNum> </ConstraintID> <ConstraintPhaseID> <eConstraintPhase>Liquid mixture 2</eConstraintPhase> </ConstraintPhaseID> <nConstraintValue>0</nConstraintValue> <nConstrDigits>0</nConstrDigits> </Constraint> <Variable> <nVarNumber>1</nVarNumber> <VariableID> <VariableType> <eTemperature>Temperature, K</eTemperature> </VariableType> </VariableID> </Variable> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>298.1</nVarValue> <nVarDigits>4</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>20417</nPropValue> <nPropDigits>5</nPropDigits> <PropUncertainty> <nUncertAssessNum>1</nUncertAssessNum> <nExpandUncertValue>13467</nExpandUncertValue> </PropUncertainty> </PropertyValue> </NumValues> </PureOrMixtureData> <PureOrMixtureData> <Component> <RegNum> <nOrgNum>1</nOrgNum> </RegNum> <nSampleNm>1</nSampleNm> </Component> <Component> <RegNum> <nOrgNum>15</nOrgNum> </RegNum> <nSampleNm>1</nSampleNm> </Component> <Component> <RegNum> <nOrgNum>17</nOrgNum> </RegNum> <nSampleNm>1</nSampleNm> </Component> <eExpPurpose>Principal objective of the work</eExpPurpose> <sCompiler>CDG</sCompiler> <sContributor>TRC</sContributor> <dateDateAdded>10/20/2004</dateDateAdded> <Property> <nPropNumber>1</nPropNumber> <Property-MethodID> <PropertyGroup> <CompositionAtPhaseEquilibrium> <ePropName>Mass concentration, kg/m3</ePropName> <eMethodName>Chromatography</eMethodName> </CompositionAtPhaseEquilibrium> </PropertyGroup> <RegNum> <nOrgNum>1</nOrgNum> </RegNum> </Property-MethodID> <PropPhaseID> <ePropPhase>Liquid mixture 1</ePropPhase> </PropPhaseID> <ePresentation>Ratio with the reference state, X/X(REF)</ePresentation> <eRefStateType>Phase in equilibrium with primary phase at the same temperature and pressure</eRefStateType> <RefPhaseID> <eRefPhase>Liquid</eRefPhase> </RefPhaseID> <PropUncertainty> <nUncertAssessNum>1</nUncertAssessNum> <sUncertEvaluator>Author</sUncertEvaluator> <nUncertLevOfConfid>95</nUncertLevOfConfid> </PropUncertainty> </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> <eComponentComposition>Mole fraction</eComponentComposition> </ConstraintType> <RegNum> <nOrgNum>1</nOrgNum> </RegNum> </ConstraintID> <ConstraintPhaseID> <eConstraintPhase>Liquid mixture 2</eConstraintPhase> </ConstraintPhaseID> <nConstraintValue>0</nConstraintValue> <nConstrDigits>0</nConstrDigits> </Constraint> <Variable> <nVarNumber>1</nVarNumber> <VariableID> <VariableType> <eTemperature>Temperature, K</eTemperature> </VariableType> </VariableID> </Variable> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>298.1</nVarValue> <nVarDigits>4</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>3236</nPropValue> <nPropDigits>4</nPropDigits> <PropUncertainty> <nUncertAssessNum>1</nUncertAssessNum> <nExpandUncertValue>566</nExpandUncertValue> </PropUncertainty> </PropertyValue> </NumValues> </PureOrMixtureData> <PureOrMixtureData> <Component> <RegNum> <nOrgNum>2</nOrgNum> </RegNum> <nSampleNm>1</nSampleNm> </Component> <Component> <RegNum> <nOrgNum>15</nOrgNum> </RegNum> <nSampleNm>1</nSampleNm> </Component> <Component> <RegNum> <nOrgNum>17</nOrgNum> </RegNum> <nSampleNm>1</nSampleNm> </Component> <eExpPurpose>Principal objective of the work</eExpPurpose> <sCompiler>CDG</sCompiler> <sContributor>TRC</sContributor> <dateDateAdded>10/20/2004</dateDateAdded> <Property> <nPropNumber>1</nPropNumber> <Property-MethodID> <PropertyGroup> <CompositionAtPhaseEquilibrium> <ePropName>Mass concentration, kg/m3</ePropName> <eMethodName>Chromatography</eMethodName> </CompositionAtPhaseEquilibrium> </PropertyGroup> <RegNum> <nOrgNum>2</nOrgNum> </RegNum> </Property-MethodID> <PropPhaseID> <ePropPhase>Liquid mixture 1</ePropPhase> </PropPhaseID> <ePresentation>Ratio with the reference state, X/X(REF)</ePresentation> <eRefStateType>Phase in equilibrium with primary phase at the same temperature and pressure</eRefStateType> <RefPhaseID> <eRefPhase>Liquid</eRefPhase> </RefPhaseID> <PropUncertainty> <nUncertAssessNum>1</nUncertAssessNum> <sUncertEvaluator>Author</sUncertEvaluator> <nUncertLevOfConfid>95</nUncertLevOfConfid> </PropUncertainty> </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> <eComponentComposition>Mole fraction</eComponentComposition> </ConstraintType> <RegNum> <nOrgNum>2</nOrgNum> </RegNum> </ConstraintID> <ConstraintPhaseID> <eConstraintPhase>Liquid mixture 2</eConstraintPhase> </ConstraintPhaseID> <nConstraintValue>0</nConstraintValue> <nConstrDigits>0</nConstrDigits> </Constraint> <Variable> <nVarNumber>1</nVarNumber> <VariableID> <VariableType> <eTemperature>Temperature, K</eTemperature> </VariableType> </VariableID> </Variable> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>298.1</nVarValue> <nVarDigits>4</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>7244</nPropValue> <nPropDigits>4</nPropDigits> <PropUncertainty> <nUncertAssessNum>1</nUncertAssessNum> <nExpandUncertValue>3227</nExpandUncertValue> </PropUncertainty> </PropertyValue> </NumValues> </PureOrMixtureData> <PureOrMixtureData> <Component> <RegNum> <nOrgNum>3</nOrgNum> </RegNum> <nSampleNm>1</nSampleNm> </Component> <Component> <RegNum> <nOrgNum>15</nOrgNum> </RegNum> <nSampleNm>1</nSampleNm> </Component> <Component> <RegNum> <nOrgNum>17</nOrgNum> </RegNum> <nSampleNm>1</nSampleNm> </Component> <eExpPurpose>Principal objective of the work</eExpPurpose> <sCompiler>CDG</sCompiler> <sContributor>TRC</sContributor> <dateDateAdded>10/20/2004</dateDateAdded> <Property> <nPropNumber>1</nPropNumber> <Property-MethodID> <PropertyGroup> <CompositionAtPhaseEquilibrium> <ePropName>Mass concentration, kg/m3</ePropName> <eMethodName>Chromatography</eMethodName> </CompositionAtPhaseEquilibrium> </PropertyGroup> <RegNum> <nOrgNum>3</nOrgNum> </RegNum> </Property-MethodID> <PropPhaseID> <ePropPhase>Liquid mixture 1</ePropPhase> </PropPhaseID> <ePresentation>Ratio with the reference state, X/X(REF)</ePresentation> <eRefStateType>Phase in equilibrium with primary phase at the same temperature and pressure</eRefStateType> <RefPhaseID> <eRefPhase>Liquid</eRefPhase> </RefPhaseID> <PropUncertainty> <nUncertAssessNum>1</nUncertAssessNum> <sUncertEvaluator>Author</sUncertEvaluator> <nUncertLevOfConfid>95</nUncertLevOfConfid> </PropUncertainty> </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> <eComponentComposition>Mole fraction</eComponentComposition> </ConstraintType> <RegNum> <nOrgNum>3</nOrgNum> </RegNum> </ConstraintID> <ConstraintPhaseID> <eConstraintPhase>Liquid mixture 2</eConstraintPhase> </ConstraintPhaseID> <nConstraintValue>0</nConstraintValue> <nConstrDigits>0</nConstrDigits> </Constraint> <Variable> <nVarNumber>1</nVarNumber> <VariableID> <VariableType> <eTemperature>Temperature, K</eTemperature> </VariableType> </VariableID> </Variable> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>298.1</nVarValue> <nVarDigits>4</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>9333</nPropValue> <nPropDigits>4</nPropDigits> <PropUncertainty> <nUncertAssessNum>1</nUncertAssessNum> <nExpandUncertValue>5122</nExpandUncertValue> </PropUncertainty> </PropertyValue> </NumValues> </PureOrMixtureData> <PureOrMixtureData> <Component> <RegNum> <nOrgNum>4</nOrgNum> </RegNum> <nSampleNm>1</nSampleNm> </Component> <Component> <RegNum> <nOrgNum>15</nOrgNum> </RegNum> <nSampleNm>1</nSampleNm> </Component> <Component> <RegNum> <nOrgNum>17</nOrgNum> </RegNum> <nSampleNm>1</nSampleNm> </Component> <eExpPurpose>Principal objective of the work</eExpPurpose> <sCompiler>CDG</sCompiler> <sContributor>TRC</sContributor> <dateDateAdded>10/20/2004</dateDateAdded> <Property> <nPropNumber>1</nPropNumber> <Property-MethodID> <PropertyGroup> <CompositionAtPhaseEquilibrium> <ePropName>Mass concentration, kg/m3</ePropName> <eMethodName>Chromatography</eMethodName> </CompositionAtPhaseEquilibrium> </PropertyGroup> <RegNum> <nOrgNum>4</nOrgNum> </RegNum> </Property-MethodID> <PropPhaseID> <ePropPhase>Liquid mixture 1</ePropPhase> </PropPhaseID> <ePresentation>Ratio with the reference state, X/X(REF)</ePresentation> <eRefStateType>Phase in equilibrium with primary phase at the same temperature and pressure</eRefStateType> <RefPhaseID> <eRefPhase>Liquid</eRefPhase> </RefPhaseID> <PropUncertainty> <nUncertAssessNum>1</nUncertAssessNum> <sUncertEvaluator>Author</sUncertEvaluator> <nUncertLevOfConfid>95</nUncertLevOfConfid> </PropUncertainty> </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> <eComponentComposition>Mole fraction</eComponentComposition> </ConstraintType> <RegNum> <nOrgNum>4</nOrgNum> </RegNum> </ConstraintID> <ConstraintPhaseID> <eConstraintPhase>Liquid mixture 2</eConstraintPhase> </ConstraintPhaseID> <nConstraintValue>0</nConstraintValue> <nConstrDigits>0</nConstrDigits> </Constraint> <Variable> <nVarNumber>1</nVarNumber> <VariableID> <VariableType> <eTemperature>Temperature, K</eTemperature> </VariableType> </VariableID> </Variable> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>298.1</nVarValue> <nVarDigits>4</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>13804</nPropValue> <nPropDigits>5</nPropDigits> <PropUncertainty> <nUncertAssessNum>1</nUncertAssessNum> <nExpandUncertValue>2414</nExpandUncertValue> </PropUncertainty> </PropertyValue> </NumValues> </PureOrMixtureData> <PureOrMixtureData> <Component> <RegNum> <nOrgNum>5</nOrgNum> </RegNum> <nSampleNm>1</nSampleNm> </Component> <Component> <RegNum> <nOrgNum>15</nOrgNum> </RegNum> <nSampleNm>1</nSampleNm> </Component> <Component> <RegNum> <nOrgNum>17</nOrgNum> </RegNum> <nSampleNm>1</nSampleNm> </Component> <eExpPurpose>Principal objective of the work</eExpPurpose> <sCompiler>CDG</sCompiler> <sContributor>TRC</sContributor> <dateDateAdded>10/20/2004</dateDateAdded> <Property> <nPropNumber>1</nPropNumber> <Property-MethodID> <PropertyGroup> <CompositionAtPhaseEquilibrium> <ePropName>Mass concentration, kg/m3</ePropName> <eMethodName>Chromatography</eMethodName> </CompositionAtPhaseEquilibrium> </PropertyGroup> <RegNum> <nOrgNum>5</nOrgNum> </RegNum> </Property-MethodID> <PropPhaseID> <ePropPhase>Liquid mixture 1</ePropPhase> </PropPhaseID> <ePresentation>Ratio with the reference state, X/X(REF)</ePresentation> <eRefStateType>Phase in equilibrium with primary phase at the same temperature and pressure</eRefStateType> <RefPhaseID> <eRefPhase>Liquid</eRefPhase> </RefPhaseID> </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> <eComponentComposition>Mole fraction</eComponentComposition> </ConstraintType> <RegNum> <nOrgNum>5</nOrgNum> </RegNum> </ConstraintID> <ConstraintPhaseID> <eConstraintPhase>Liquid mixture 2</eConstraintPhase> </ConstraintPhaseID> <nConstraintValue>0</nConstraintValue> <nConstrDigits>0</nConstrDigits> </Constraint> <Variable> <nVarNumber>1</nVarNumber> <VariableID> <VariableType> <eTemperature>Temperature, K</eTemperature> </VariableType> </VariableID> </Variable> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>298.1</nVarValue> <nVarDigits>4</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>13183</nPropValue> <nPropDigits>5</nPropDigits> </PropertyValue> </NumValues> </PureOrMixtureData> <PureOrMixtureData> <Component> <RegNum> <nOrgNum>6</nOrgNum> </RegNum> <nSampleNm>1</nSampleNm> </Component> <Component> <RegNum> <nOrgNum>15</nOrgNum> </RegNum> <nSampleNm>1</nSampleNm> </Component> <Component> <RegNum> <nOrgNum>17</nOrgNum> </RegNum> <nSampleNm>1</nSampleNm> </Component> <eExpPurpose>Principal objective of the work</eExpPurpose> <sCompiler>CDG</sCompiler> <sContributor>TRC</sContributor> <dateDateAdded>10/20/2004</dateDateAdded> <Property> <nPropNumber>1</nPropNumber> <Property-MethodID> <PropertyGroup> <CompositionAtPhaseEquilibrium> <ePropName>Mass concentration, kg/m3</ePropName> <eMethodName>Chromatography</eMethodName> </CompositionAtPhaseEquilibrium> </PropertyGroup> <RegNum> <nOrgNum>6</nOrgNum> </RegNum> </Property-MethodID> <PropPhaseID> <ePropPhase>Liquid mixture 1</ePropPhase> </PropPhaseID> <ePresentation>Ratio with the reference state, X/X(REF)</ePresentation> <eRefStateType>Phase in equilibrium with primary phase at the same temperature and pressure</eRefStateType> <RefPhaseID> <eRefPhase>Liquid</eRefPhase> </RefPhaseID> <PropUncertainty> <nUncertAssessNum>1</nUncertAssessNum> <sUncertEvaluator>Author</sUncertEvaluator> <nUncertLevOfConfid>95</nUncertLevOfConfid> </PropUncertainty> </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> <eComponentComposition>Mole fraction</eComponentComposition> </ConstraintType> <RegNum> <nOrgNum>6</nOrgNum> </RegNum> </ConstraintID> <ConstraintPhaseID> <eConstraintPhase>Liquid mixture 2</eConstraintPhase> </ConstraintPhaseID> <nConstraintValue>0</nConstraintValue> <nConstrDigits>0</nConstrDigits> </Constraint> <Variable> <nVarNumber>1</nVarNumber> <VariableID> <VariableType> <eTemperature>Temperature, K</eTemperature> </VariableType> </VariableID> </Variable> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>298.1</nVarValue> <nVarDigits>4</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>16982</nPropValue> <nPropDigits>5</nPropDigits> <PropUncertainty> <nUncertAssessNum>1</nUncertAssessNum> <nExpandUncertValue>8136</nExpandUncertValue> </PropUncertainty> </PropertyValue> </NumValues> </PureOrMixtureData> <PureOrMixtureData> <Component> <RegNum> <nOrgNum>7</nOrgNum> </RegNum> <nSampleNm>1</nSampleNm> </Component> <Component> <RegNum> <nOrgNum>15</nOrgNum> </RegNum> <nSampleNm>1</nSampleNm> </Component> <Component> <RegNum> <nOrgNum>17</nOrgNum> </RegNum> <nSampleNm>1</nSampleNm> </Component> <eExpPurpose>Principal objective of the work</eExpPurpose> <sCompiler>CDG</sCompiler> <sContributor>TRC</sContributor> <dateDateAdded>10/20/2004</dateDateAdded> <Property> <nPropNumber>1</nPropNumber> <Property-MethodID> <PropertyGroup> <CompositionAtPhaseEquilibrium> <ePropName>Mass concentration, kg/m3</ePropName> <eMethodName>Chromatography</eMethodName> </CompositionAtPhaseEquilibrium> </PropertyGroup> <RegNum> <nOrgNum>7</nOrgNum> </RegNum> </Property-MethodID> <PropPhaseID> <ePropPhase>Liquid mixture 1</ePropPhase> </PropPhaseID> <ePresentation>Ratio with the reference state, X/X(REF)</ePresentation> <eRefStateType>Phase in equilibrium with primary phase at the same temperature and pressure</eRefStateType> <RefPhaseID> <eRefPhase>Liquid</eRefPhase> </RefPhaseID> <PropUncertainty> <nUncertAssessNum>1</nUncertAssessNum> <sUncertEvaluator>Author</sUncertEvaluator> <nUncertLevOfConfid>95</nUncertLevOfConfid> </PropUncertainty> </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> <eComponentComposition>Mole fraction</eComponentComposition> </ConstraintType> <RegNum> <nOrgNum>7</nOrgNum> </RegNum> </ConstraintID> <ConstraintPhaseID> <eConstraintPhase>Liquid mixture 2</eConstraintPhase> </ConstraintPhaseID> <nConstraintValue>0</nConstraintValue> <nConstrDigits>0</nConstrDigits> </Constraint> <Variable> <nVarNumber>1</nVarNumber> <VariableID> <VariableType> <eTemperature>Temperature, K</eTemperature> </VariableType> </VariableID> </Variable> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>298.1</nVarValue> <nVarDigits>4</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>16218</nPropValue> <nPropDigits>5</nPropDigits> <PropUncertainty> <nUncertAssessNum>1</nUncertAssessNum> <nExpandUncertValue>9486</nExpandUncertValue> </PropUncertainty> </PropertyValue> </NumValues> </PureOrMixtureData> <PureOrMixtureData> <Component> <RegNum> <nOrgNum>8</nOrgNum> </RegNum> <nSampleNm>1</nSampleNm> </Component> <Component> <RegNum> <nOrgNum>15</nOrgNum> </RegNum> <nSampleNm>1</nSampleNm> </Component> <Component> <RegNum> <nOrgNum>17</nOrgNum> </RegNum> <nSampleNm>1</nSampleNm> </Component> <eExpPurpose>Principal objective of the work</eExpPurpose> <sCompiler>CDG</sCompiler> <sContributor>TRC</sContributor> <dateDateAdded>10/20/2004</dateDateAdded> <Property> <nPropNumber>1</nPropNumber> <Property-MethodID> <PropertyGroup> <CompositionAtPhaseEquilibrium> <ePropName>Mass concentration, kg/m3</ePropName> <eMethodName>Chromatography</eMethodName> </CompositionAtPhaseEquilibrium> </PropertyGroup> <RegNum> <nOrgNum>8</nOrgNum> </RegNum> </Property-MethodID> <PropPhaseID> <ePropPhase>Liquid mixture 1</ePropPhase> </PropPhaseID> <ePresentation>Ratio with the reference state, X/X(REF)</ePresentation> <eRefStateType>Phase in equilibrium with primary phase at the same temperature and pressure</eRefStateType> <RefPhaseID> <eRefPhase>Liquid</eRefPhase> </RefPhaseID> <PropUncertainty> <nUncertAssessNum>1</nUncertAssessNum> <sUncertEvaluator>Author</sUncertEvaluator> <nUncertLevOfConfid>95</nUncertLevOfConfid> </PropUncertainty> </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> <eComponentComposition>Mole fraction</eComponentComposition> </ConstraintType> <RegNum> <nOrgNum>8</nOrgNum> </RegNum> </ConstraintID> <ConstraintPhaseID> <eConstraintPhase>Liquid mixture 2</eConstraintPhase> </ConstraintPhaseID> <nConstraintValue>0</nConstraintValue> <nConstrDigits>0</nConstrDigits> </Constraint> <Variable> <nVarNumber>1</nVarNumber> <VariableID> <VariableType> <eTemperature>Temperature, K</eTemperature> </VariableType> </VariableID> </Variable> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>298.1</nVarValue> <nVarDigits>4</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>14791</nPropValue> <nPropDigits>5</nPropDigits> <PropUncertainty> <nUncertAssessNum>1</nUncertAssessNum> <nExpandUncertValue>5626</nExpandUncertValue> </PropUncertainty> </PropertyValue> </NumValues> </PureOrMixtureData> <PureOrMixtureData> <Component> <RegNum> <nOrgNum>9</nOrgNum> </RegNum> <nSampleNm>1</nSampleNm> </Component> <Component> <RegNum> <nOrgNum>15</nOrgNum> </RegNum> <nSampleNm>1</nSampleNm> </Component> <Component> <RegNum> <nOrgNum>17</nOrgNum> </RegNum> <nSampleNm>1</nSampleNm> </Component> <eExpPurpose>Principal objective of the work</eExpPurpose> <sCompiler>CDG</sCompiler> <sContributor>TRC</sContributor> <dateDateAdded>10/20/2004</dateDateAdded> <Property> <nPropNumber>1</nPropNumber> <Property-MethodID> <PropertyGroup> <CompositionAtPhaseEquilibrium> <ePropName>Mass concentration, kg/m3</ePropName> <eMethodName>Chromatography</eMethodName> </CompositionAtPhaseEquilibrium> </PropertyGroup> <RegNum> <nOrgNum>9</nOrgNum> </RegNum> </Property-MethodID> <PropPhaseID> <ePropPhase>Liquid mixture 1</ePropPhase> </PropPhaseID> <ePresentation>Ratio with the reference state, X/X(REF)</ePresentation> <eRefStateType>Phase in equilibrium with primary phase at the same temperature and pressure</eRefStateType> <RefPhaseID> <eRefPhase>Liquid</eRefPhase> </RefPhaseID> <PropUncertainty> <nUncertAssessNum>1</nUncertAssessNum> <sUncertEvaluator>Author</sUncertEvaluator> <nUncertLevOfConfid>95</nUncertLevOfConfid> </PropUncertainty> </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> <eComponentComposition>Mole fraction</eComponentComposition> </ConstraintType> <RegNum> <nOrgNum>9</nOrgNum> </RegNum> </ConstraintID> <ConstraintPhaseID> <eConstraintPhase>Liquid mixture 2</eConstraintPhase> </ConstraintPhaseID> <nConstraintValue>0</nConstraintValue> <nConstrDigits>0</nConstrDigits> </Constraint> <Variable> <nVarNumber>1</nVarNumber> <VariableID> <VariableType> <eTemperature>Temperature, K</eTemperature> </VariableType> </VariableID> </Variable> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>298.1</nVarValue> <nVarDigits>4</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>16982</nPropValue> <nPropDigits>5</nPropDigits> <PropUncertainty> <nUncertAssessNum>1</nUncertAssessNum> <nExpandUncertValue>8722</nExpandUncertValue> </PropUncertainty> </PropertyValue> </NumValues> </PureOrMixtureData> <PureOrMixtureData> <Component> <RegNum> <nOrgNum>10</nOrgNum> </RegNum> <nSampleNm>1</nSampleNm> </Component> <Component> <RegNum> <nOrgNum>15</nOrgNum> </RegNum> <nSampleNm>1</nSampleNm> </Component> <Component> <RegNum> <nOrgNum>17</nOrgNum> </RegNum> <nSampleNm>1</nSampleNm> </Component> <eExpPurpose>Principal objective of the work</eExpPurpose> <sCompiler>CDG</sCompiler> <sContributor>TRC</sContributor> <dateDateAdded>10/20/2004</dateDateAdded> <Property> <nPropNumber>1</nPropNumber> <Property-MethodID> <PropertyGroup> <CompositionAtPhaseEquilibrium> <ePropName>Mass concentration, kg/m3</ePropName> <eMethodName>Chromatography</eMethodName> </CompositionAtPhaseEquilibrium> </PropertyGroup> <RegNum> <nOrgNum>10</nOrgNum> </RegNum> </Property-MethodID> <PropPhaseID> <ePropPhase>Liquid mixture 1</ePropPhase> </PropPhaseID> <ePresentation>Ratio with the reference state, X/X(REF)</ePresentation> <eRefStateType>Phase in equilibrium with primary phase at the same temperature and pressure</eRefStateType> <RefPhaseID> <eRefPhase>Liquid</eRefPhase> </RefPhaseID> <PropUncertainty> <nUncertAssessNum>1</nUncertAssessNum> <sUncertEvaluator>Author</sUncertEvaluator> <nUncertLevOfConfid>95</nUncertLevOfConfid> </PropUncertainty> </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> <eComponentComposition>Mole fraction</eComponentComposition> </ConstraintType> <RegNum> <nOrgNum>10</nOrgNum> </RegNum> </ConstraintID> <ConstraintPhaseID> <eConstraintPhase>Liquid mixture 2</eConstraintPhase> </ConstraintPhaseID> <nConstraintValue>0</nConstraintValue> <nConstrDigits>0</nConstrDigits> </Constraint> <Variable> <nVarNumber>1</nVarNumber> <VariableID> <VariableType> <eTemperature>Temperature, K</eTemperature> </VariableType> </VariableID> </Variable> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>298.1</nVarValue> <nVarDigits>4</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>18197</nPropValue> <nPropDigits>5</nPropDigits> <PropUncertainty> <nUncertAssessNum>1</nUncertAssessNum> <nExpandUncertValue>9345</nExpandUncertValue> </PropUncertainty> </PropertyValue> </NumValues> </PureOrMixtureData> <PureOrMixtureData> <Component> <RegNum> <nOrgNum>11</nOrgNum> </RegNum> <nSampleNm>1</nSampleNm> </Component> <Component> <RegNum> <nOrgNum>15</nOrgNum> </RegNum> <nSampleNm>1</nSampleNm> </Component> <Component> <RegNum> <nOrgNum>17</nOrgNum> </RegNum> <nSampleNm>1</nSampleNm> </Component> <eExpPurpose>Principal objective of the work</eExpPurpose> <sCompiler>CDG</sCompiler> <sContributor>TRC</sContributor> <dateDateAdded>10/20/2004</dateDateAdded> <Property> <nPropNumber>1</nPropNumber> <Property-MethodID> <PropertyGroup> <CompositionAtPhaseEquilibrium> <ePropName>Mass concentration, kg/m3</ePropName> <eMethodName>Chromatography</eMethodName> </CompositionAtPhaseEquilibrium> </PropertyGroup> <RegNum> <nOrgNum>11</nOrgNum> </RegNum> </Property-MethodID> <PropPhaseID> <ePropPhase>Liquid mixture 1</ePropPhase> </PropPhaseID> <ePresentation>Ratio with the reference state, X/X(REF)</ePresentation> <eRefStateType>Phase in equilibrium with primary phase at the same temperature and pressure</eRefStateType> <RefPhaseID> <eRefPhase>Liquid</eRefPhase> </RefPhaseID> <PropUncertainty> <nUncertAssessNum>1</nUncertAssessNum> <sUncertEvaluator>Author</sUncertEvaluator> <nUncertLevOfConfid>95</nUncertLevOfConfid> </PropUncertainty> </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> <eComponentComposition>Mole fraction</eComponentComposition> </ConstraintType> <RegNum> <nOrgNum>11</nOrgNum> </RegNum> </ConstraintID> <ConstraintPhaseID> <eConstraintPhase>Liquid mixture 2</eConstraintPhase> </ConstraintPhaseID> <nConstraintValue>0</nConstraintValue> <nConstrDigits>0</nConstrDigits> </Constraint> <Variable> <nVarNumber>1</nVarNumber> <VariableID> <VariableType> <eTemperature>Temperature, K</eTemperature> </VariableType> </VariableID> </Variable> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>298.1</nVarValue> <nVarDigits>4</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>16596</nPropValue> <nPropDigits>5</nPropDigits> <PropUncertainty> <nUncertAssessNum>1</nUncertAssessNum> <nExpandUncertValue>9108</nExpandUncertValue> </PropUncertainty> </PropertyValue> </NumValues> </PureOrMixtureData> <PureOrMixtureData> <Component> <RegNum> <nOrgNum>12</nOrgNum> </RegNum> <nSampleNm>1</nSampleNm> </Component> <Component> <RegNum> <nOrgNum>15</nOrgNum> </RegNum> <nSampleNm>1</nSampleNm> </Component> <Component> <RegNum> <nOrgNum>17</nOrgNum> </RegNum> <nSampleNm>1</nSampleNm> </Component> <eExpPurpose>Principal objective of the work</eExpPurpose> <sCompiler>CDG</sCompiler> <sContributor>TRC</sContributor> <dateDateAdded>10/20/2004</dateDateAdded> <Property> <nPropNumber>1</nPropNumber> <Property-MethodID> <PropertyGroup> <CompositionAtPhaseEquilibrium> <ePropName>Mass concentration, kg/m3</ePropName> <eMethodName>Chromatography</eMethodName> </CompositionAtPhaseEquilibrium> </PropertyGroup> <RegNum> <nOrgNum>12</nOrgNum> </RegNum> </Property-MethodID> <PropPhaseID> <ePropPhase>Liquid mixture 1</ePropPhase> </PropPhaseID> <ePresentation>Ratio with the reference state, X/X(REF)</ePresentation> <eRefStateType>Phase in equilibrium with primary phase at the same temperature and pressure</eRefStateType> <RefPhaseID> <eRefPhase>Liquid</eRefPhase> </RefPhaseID> <PropUncertainty> <nUncertAssessNum>1</nUncertAssessNum> <sUncertEvaluator>Author</sUncertEvaluator> <nUncertLevOfConfid>95</nUncertLevOfConfid> </PropUncertainty> </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> <eComponentComposition>Mole fraction</eComponentComposition> </ConstraintType> <RegNum> <nOrgNum>12</nOrgNum> </RegNum> </ConstraintID> <ConstraintPhaseID> <eConstraintPhase>Liquid mixture 2</eConstraintPhase> </ConstraintPhaseID> <nConstraintValue>0</nConstraintValue> <nConstrDigits>0</nConstrDigits> </Constraint> <Variable> <nVarNumber>1</nVarNumber> <VariableID> <VariableType> <eTemperature>Temperature, K</eTemperature> </VariableType> </VariableID> </Variable> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>298.1</nVarValue> <nVarDigits>4</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>20893</nPropValue> <nPropDigits>5</nPropDigits> <PropUncertainty> <nUncertAssessNum>1</nUncertAssessNum> <nExpandUncertValue>9307</nExpandUncertValue> </PropUncertainty> </PropertyValue> </NumValues> </PureOrMixtureData> <PureOrMixtureData> <Component> <RegNum> <nOrgNum>13</nOrgNum> </RegNum> <nSampleNm>1</nSampleNm> </Component> <Component> <RegNum> <nOrgNum>15</nOrgNum> </RegNum> <nSampleNm>1</nSampleNm> </Component> <Component> <RegNum> <nOrgNum>17</nOrgNum> </RegNum> <nSampleNm>1</nSampleNm> </Component> <eExpPurpose>Principal objective of the work</eExpPurpose> <sCompiler>CDG</sCompiler> <sContributor>TRC</sContributor> <dateDateAdded>10/20/2004</dateDateAdded> <Property> <nPropNumber>1</nPropNumber> <Property-MethodID> <PropertyGroup> <CompositionAtPhaseEquilibrium> <ePropName>Mass concentration, kg/m3</ePropName> <eMethodName>Chromatography</eMethodName> </CompositionAtPhaseEquilibrium> </PropertyGroup> <RegNum> <nOrgNum>13</nOrgNum> </RegNum> </Property-MethodID> <PropPhaseID> <ePropPhase>Liquid mixture 1</ePropPhase> </PropPhaseID> <ePresentation>Ratio with the reference state, X/X(REF)</ePresentation> <eRefStateType>Phase in equilibrium with primary phase at the same temperature and pressure</eRefStateType> <RefPhaseID> <eRefPhase>Liquid</eRefPhase> </RefPhaseID> <PropUncertainty> <nUncertAssessNum>1</nUncertAssessNum> <sUncertEvaluator>Author</sUncertEvaluator> <nUncertLevOfConfid>95</nUncertLevOfConfid> </PropUncertainty> </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> <eComponentComposition>Mole fraction</eComponentComposition> </ConstraintType> <RegNum> <nOrgNum>13</nOrgNum> </RegNum> </ConstraintID> <ConstraintPhaseID> <eConstraintPhase>Liquid mixture 2</eConstraintPhase> </ConstraintPhaseID> <nConstraintValue>0</nConstraintValue> <nConstrDigits>0</nConstrDigits> </Constraint> <Variable> <nVarNumber>1</nVarNumber> <VariableID> <VariableType> <eTemperature>Temperature, K</eTemperature> </VariableType> </VariableID> </Variable> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>298.1</nVarValue> <nVarDigits>4</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>16982</nPropValue> <nPropDigits>5</nPropDigits> <PropUncertainty> <nUncertAssessNum>1</nUncertAssessNum> <nExpandUncertValue>8722</nExpandUncertValue> </PropUncertainty> </PropertyValue> </NumValues> </PureOrMixtureData> <PureOrMixtureData> <Component> <RegNum> <nOrgNum>14</nOrgNum> </RegNum> <nSampleNm>1</nSampleNm> </Component> <Component> <RegNum> <nOrgNum>15</nOrgNum> </RegNum> <nSampleNm>1</nSampleNm> </Component> <Component> <RegNum> <nOrgNum>17</nOrgNum> </RegNum> <nSampleNm>1</nSampleNm> </Component> <eExpPurpose>Principal objective of the work</eExpPurpose> <sCompiler>CDG</sCompiler> <sContributor>TRC</sContributor> <dateDateAdded>10/20/2004</dateDateAdded> <Property> <nPropNumber>1</nPropNumber> <Property-MethodID> <PropertyGroup> <CompositionAtPhaseEquilibrium> <ePropName>Mass concentration, kg/m3</ePropName> <eMethodName>Chromatography</eMethodName> </CompositionAtPhaseEquilibrium> </PropertyGroup> <RegNum> <nOrgNum>14</nOrgNum> </RegNum> </Property-MethodID> <PropPhaseID> <ePropPhase>Liquid mixture 1</ePropPhase> </PropPhaseID> <ePresentation>Ratio with the reference state, X/X(REF)</ePresentation> <eRefStateType>Phase in equilibrium with primary phase at the same temperature and pressure</eRefStateType> <RefPhaseID> <eRefPhase>Liquid</eRefPhase> </RefPhaseID> <PropUncertainty> <nUncertAssessNum>1</nUncertAssessNum> <sUncertEvaluator>Author</sUncertEvaluator> <nUncertLevOfConfid>95</nUncertLevOfConfid> </PropUncertainty> </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> <eComponentComposition>Mole fraction</eComponentComposition> </ConstraintType> <RegNum> <nOrgNum>14</nOrgNum> </RegNum> </ConstraintID> <ConstraintPhaseID> <eConstraintPhase>Liquid mixture 2</eConstraintPhase> </ConstraintPhaseID> <nConstraintValue>0</nConstraintValue> <nConstrDigits>0</nConstrDigits> </Constraint> <Variable> <nVarNumber>1</nVarNumber> <VariableID> <VariableType> <eTemperature>Temperature, K</eTemperature> </VariableType> </VariableID> </Variable> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>298.1</nVarValue> <nVarDigits>4</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>19953</nPropValue> <nPropDigits>5</nPropDigits> <PropUncertainty> <nUncertAssessNum>1</nUncertAssessNum> <nExpandUncertValue>10247</nExpandUncertValue> </PropUncertainty> </PropertyValue> </NumValues> </PureOrMixtureData> <PureOrMixtureData> <Component> <RegNum> <nOrgNum>18</nOrgNum> </RegNum> <nSampleNm>1</nSampleNm> </Component> <Component> <RegNum> <nOrgNum>15</nOrgNum> </RegNum> <nSampleNm>1</nSampleNm> </Component> <Component> <RegNum> <nOrgNum>16</nOrgNum> </RegNum> <nSampleNm>1</nSampleNm> </Component> <eExpPurpose>Principal objective of the work</eExpPurpose> <sCompiler>JCE</sCompiler> <sContributor>JCE</sContributor> <dateDateAdded>10/28/2004</dateDateAdded> <Property> <nPropNumber>1</nPropNumber> <Property-MethodID> <PropertyGroup> <CompositionAtPhaseEquilibrium> <ePropName>Mass concentration, kg/m3</ePropName> <eMethodName>Chromatography</eMethodName> </CompositionAtPhaseEquilibrium> </PropertyGroup> <RegNum> <nOrgNum>18</nOrgNum> </RegNum> </Property-MethodID> <PropPhaseID> <ePropPhase>Liquid mixture 1</ePropPhase> </PropPhaseID> <ePresentation>Ratio with the reference state, X/X(REF)</ePresentation> <eRefStateType>Phase in equilibrium with primary phase at the same temperature and pressure</eRefStateType> <RefPhaseID> <eRefPhase>Liquid</eRefPhase> </RefPhaseID> <PropUncertainty> <nUncertAssessNum>1</nUncertAssessNum> <sUncertEvaluator>Author</sUncertEvaluator> <nUncertLevOfConfid>95</nUncertLevOfConfid> </PropUncertainty> </Property> <PhaseID> <ePhase>Liquid mixture 1</ePhase> </PhaseID> <PhaseID> <ePhase>Liquid mixture 2</ePhase> </PhaseID> <Constraint> <ConstraintID> <ConstraintType> <eComponentComposition>Mole fraction</eComponentComposition> </ConstraintType> <RegNum> <nOrgNum>18</nOrgNum> </RegNum> </ConstraintID> <ConstraintPhaseID> <eConstraintPhase>Liquid mixture 2</eConstraintPhase> </ConstraintPhaseID> <nConstraintValue>0</nConstraintValue> <nConstrDigits>0</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> <eTemperature>Temperature, K</eTemperature> </VariableType> </VariableID> </Variable> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>298.1</nVarValue> <nVarDigits>4</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>22909</nPropValue> <nPropDigits>5</nPropDigits> <PropUncertainty> <nUncertAssessNum>1</nUncertAssessNum> <nExpandUncertValue>10976</nExpandUncertValue> </PropUncertainty> </PropertyValue> </NumValues> </PureOrMixtureData> <PureOrMixtureData> <Component> <RegNum> <nOrgNum>18</nOrgNum> </RegNum> <nSampleNm>1</nSampleNm> </Component> <Component> <RegNum> <nOrgNum>15</nOrgNum> </RegNum> <nSampleNm>1</nSampleNm> </Component> <Component> <RegNum> <nOrgNum>17</nOrgNum> </RegNum> <nSampleNm>1</nSampleNm> </Component> <eExpPurpose>Principal objective of the work</eExpPurpose> <sCompiler>JCE</sCompiler> <sContributor>JCE</sContributor> <dateDateAdded>10/28/2004</dateDateAdded> <Property> <nPropNumber>1</nPropNumber> <Property-MethodID> <PropertyGroup> <CompositionAtPhaseEquilibrium> <ePropName>Mass concentration, kg/m3</ePropName> <eMethodName>Chromatography</eMethodName> </CompositionAtPhaseEquilibrium> </PropertyGroup> <RegNum> <nOrgNum>18</nOrgNum> </RegNum> </Property-MethodID> <PropPhaseID> <ePropPhase>Liquid mixture 1</ePropPhase> </PropPhaseID> <ePresentation>Ratio with the reference state, X/X(REF)</ePresentation> <eRefStateType>Phase in equilibrium with primary phase at the same temperature and pressure</eRefStateType> <RefPhaseID> <eRefPhase>Liquid</eRefPhase> </RefPhaseID> <PropUncertainty> <nUncertAssessNum>1</nUncertAssessNum> <sUncertEvaluator>Author</sUncertEvaluator> <nUncertLevOfConfid>95</nUncertLevOfConfid> </PropUncertainty> </Property> <PhaseID> <ePhase>Liquid mixture 1</ePhase> </PhaseID> <PhaseID> <ePhase>Liquid mixture 2</ePhase> </PhaseID> <Constraint> <ConstraintID> <ConstraintType> <eComponentComposition>Mole fraction</eComponentComposition> </ConstraintType> <RegNum> <nOrgNum>18</nOrgNum> </RegNum> </ConstraintID> <ConstraintPhaseID> <eConstraintPhase>Liquid mixture 2</eConstraintPhase> </ConstraintPhaseID> <nConstraintValue>0</nConstraintValue> <nConstrDigits>0</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> <eTemperature>Temperature, K</eTemperature> </VariableType> </VariableID> </Variable> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>298.1</nVarValue> <nVarDigits>4</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>20417</nPropValue> <nPropDigits>5</nPropDigits> <PropUncertainty> <nUncertAssessNum>1</nUncertAssessNum> <nExpandUncertValue>10486</nExpandUncertValue> </PropUncertainty> </PropertyValue> </NumValues> </PureOrMixtureData> </DataReport>

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