ThermoML Data file

Right click here and Save Target to download the xml file

Information on ThermoML

<?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>hua</sAuthor1> <sAuthor2>ouy</sAuthor2> <nAuthorn>0</nAuthorn> </TRCRefID> <eType>journal</eType> <eSourceType>Original</eSourceType> <sAuthor>Huang, Z.[Zhongqi]</sAuthor> <sAuthor>Ouyang, G.[Gangfeng]</sAuthor> <sAuthor>Liu, F.[Faqiang]</sAuthor> <sAuthor>Xu, Z.[Zhuyuan]</sAuthor> <sAuthor>Zhang, X.[Xiliang]</sAuthor> <sAuthor>Zhang, W.[Weiqing]</sAuthor> <sPubName>J. Chem. Eng. Data</sPubName> <yrPubYr>2003</yrPubYr> <dateCit>2003-11-17</dateCit> <sTitle>Solid and Liquid Phase Equilibria in Mixtures of 1,8-Cineole with Phenol, Cyclohexanol, and an n-Alkanol</sTitle> <sAbstract>Solid-liquid phase diagrams have been constructed for 1,8-cineole with phenol or cyclohexanol or an n-alkanol. Solid addition compounds with the empirical formulas C10H18O*C6H5OH and C10H18O*C6H11OH were formed. Compound formation is attributed to hydrogen bonding. No solid addition compounds form in (1,8-cineole + methanol, + ethanol, + 1-propanol, or + 1-butanol).</sAbstract> <sKeyword>(Solid + liquid) equilibrium</sKeyword> <sKeyword>Solid-compound</sKeyword> <sKeyword>1</sKeyword> <sKeyword>8-cineole</sKeyword> <sVol>48</sVol> <sPage>1521-1523</sPage> </Citation> <Compound> <RegNum> <nOrgNum>1</nOrgNum> </RegNum> <sCommonName>1,8-cineole</sCommonName> <sFormulaMolec>C10H18O</sFormulaMolec> <Sample> <nSampleNm>1</nSampleNm> <eSource>Commercial source</eSource> <purity> <nStep>1</nStep> <nPurityMol>99</nPurityMol> <nPurityMolDigits>2</nPurityMolDigits> <eAnalMeth>Gas chromatography</eAnalMeth> </purity> <purity> <nStep>2</nStep> <ePurifMethod>Fractional distillation</ePurifMethod> </purity> <purity> <nStep>2</nStep> <nPurityMol>99.72</nPurityMol> <nPurityMolDigits>4</nPurityMolDigits> <eAnalMeth>Gas chromatography</eAnalMeth> </purity> </Sample> </Compound> <Compound> <RegNum> <nOrgNum>2</nOrgNum> </RegNum> <sCommonName>phenol</sCommonName> <sFormulaMolec>C6H6O</sFormulaMolec> <Sample> <nSampleNm>1</nSampleNm> <eSource>Commercial source</eSource> <purity> <nStep>1</nStep> <nPurityMol>99.5</nPurityMol> <nPurityMolDigits>3</nPurityMolDigits> <eAnalMeth>Gas chromatography</eAnalMeth> </purity> <purity> <nStep>2</nStep> <ePurifMethod>Fractional distillation</ePurifMethod> </purity> <purity> <nStep>2</nStep> <nPurityMol>99.67</nPurityMol> <nPurityMolDigits>4</nPurityMolDigits> <eAnalMeth>Gas chromatography</eAnalMeth> </purity> </Sample> </Compound> <Compound> <RegNum> <nOrgNum>3</nOrgNum> </RegNum> <sCommonName>cyclohexanol</sCommonName> <sFormulaMolec>C6H12O</sFormulaMolec> <Sample> <nSampleNm>1</nSampleNm> <eSource>Commercial source</eSource> <purity> <nStep>1</nStep> <nPurityMol>99.5</nPurityMol> <nPurityMolDigits>3</nPurityMolDigits> <eAnalMeth>Gas chromatography</eAnalMeth> </purity> <purity> <nStep>2</nStep> <ePurifMethod>Fractional distillation</ePurifMethod> </purity> <purity> <nStep>2</nStep> <nPurityMol>99.75</nPurityMol> <nPurityMolDigits>4</nPurityMolDigits> <eAnalMeth>Gas chromatography</eAnalMeth> </purity> </Sample> </Compound> <Compound> <RegNum> <nOrgNum>4</nOrgNum> </RegNum> <sCommonName>methanol</sCommonName> <sFormulaMolec>CH4O</sFormulaMolec> <Sample> <nSampleNm>1</nSampleNm> <eSource>Commercial source</eSource> <purity> <nStep>1</nStep> <nPurityMol>99.5</nPurityMol> <nPurityMolDigits>3</nPurityMolDigits> <eAnalMeth>Gas chromatography</eAnalMeth> </purity> <purity> <nStep>2</nStep> <ePurifMethod>Fractional distillation</ePurifMethod> </purity> <purity> <nStep>2</nStep> <nPurityMol>99.95</nPurityMol> <nPurityMolDigits>4</nPurityMolDigits> <eAnalMeth>Gas chromatography</eAnalMeth> </purity> </Sample> </Compound> <Compound> <RegNum> <nOrgNum>5</nOrgNum> </RegNum> <sCommonName>ethanol</sCommonName> <sFormulaMolec>C2H6O</sFormulaMolec> <Sample> <nSampleNm>1</nSampleNm> <eSource>Commercial source</eSource> <purity> <nStep>1</nStep> <nPurityMol>99.5</nPurityMol> <nPurityMolDigits>3</nPurityMolDigits> <eAnalMeth>Gas chromatography</eAnalMeth> </purity> <purity> <nStep>2</nStep> <ePurifMethod>Fractional distillation</ePurifMethod> </purity> <purity> <nStep>2</nStep> <nPurityMol>99.97</nPurityMol> <nPurityMolDigits>4</nPurityMolDigits> <eAnalMeth>Gas chromatography</eAnalMeth> </purity> </Sample> </Compound> <Compound> <RegNum> <nOrgNum>6</nOrgNum> </RegNum> <sCommonName>1-propanol</sCommonName> <sFormulaMolec>C3H8O</sFormulaMolec> <Sample> <nSampleNm>1</nSampleNm> <eSource>Commercial source</eSource> <purity> <nStep>1</nStep> <nPurityMol>99.5</nPurityMol> <nPurityMolDigits>3</nPurityMolDigits> <eAnalMeth>Gas chromatography</eAnalMeth> </purity> <purity> <nStep>2</nStep> <ePurifMethod>Fractional distillation</ePurifMethod> </purity> <purity> <nStep>2</nStep> <nPurityMol>99.98</nPurityMol> <nPurityMolDigits>4</nPurityMolDigits> <eAnalMeth>Gas chromatography</eAnalMeth> </purity> </Sample> </Compound> <Compound> <RegNum> <nOrgNum>7</nOrgNum> </RegNum> <sCommonName>1-butanol</sCommonName> <sFormulaMolec>C4H10O</sFormulaMolec> <Sample> <nSampleNm>1</nSampleNm> <eSource>Commercial source</eSource> <purity> <nStep>1</nStep> <nPurityMol>99.5</nPurityMol> <nPurityMolDigits>3</nPurityMolDigits> <eAnalMeth>Gas chromatography</eAnalMeth> </purity> <purity> <nStep>2</nStep> <ePurifMethod>Fractional distillation</ePurifMethod> </purity> <purity> <nStep>2</nStep> <nPurityMol>99.99</nPurityMol> <nPurityMolDigits>4</nPurityMolDigits> <eAnalMeth>Gas chromatography</eAnalMeth> </purity> </Sample> </Compound> <PureOrMixtureData> <Component> <RegNum> <nOrgNum>1</nOrgNum> </RegNum> <nSampleNm>1</nSampleNm> </Component> <eExpPurpose>Principal objective of the work</eExpPurpose> <sCompiler>RDC</sCompiler> <sContributor>TRC</sContributor> <dateDateAdded>11/14/2003</dateDateAdded> <Property> <nPropNumber>1</nPropNumber> <Property-MethodID> <PropertyGroup> <PhaseTransition> <ePropName>Solid-liquid equilibrium temperature, K</ePropName> <eMethodName>Visual observation</eMethodName> </PhaseTransition> </PropertyGroup> </Property-MethodID> <PropPhaseID> <ePropPhase>Liquid</ePropPhase> </PropPhaseID> <ePresentation>Direct value, X</ePresentation> </Property> <PhaseID> <ePhase>Liquid</ePhase> </PhaseID> <PhaseID> <ePhase>Crystal</ePhase> </PhaseID> <Variable> <nVarNumber>1</nVarNumber> <VariableID> <VariableType> <ePressure>Pressure, kPa</ePressure> </VariableType> </VariableID> </Variable> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>101.3</nVarValue> <nVarDigits>4</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>274.42</nPropValue> <nPropDigits>5</nPropDigits> </PropertyValue> </NumValues> </PureOrMixtureData> <PureOrMixtureData> <Component> <RegNum> <nOrgNum>2</nOrgNum> </RegNum> <nSampleNm>1</nSampleNm> </Component> <eExpPurpose>Principal objective of the work</eExpPurpose> <sCompiler>RDC</sCompiler> <sContributor>TRC</sContributor> <dateDateAdded>11/14/2003</dateDateAdded> <Property> <nPropNumber>1</nPropNumber> <Property-MethodID> <PropertyGroup> <PhaseTransition> <ePropName>Solid-liquid equilibrium temperature, K</ePropName> <eMethodName>Visual observation</eMethodName> </PhaseTransition> </PropertyGroup> </Property-MethodID> <PropPhaseID> <ePropPhase>Liquid</ePropPhase> </PropPhaseID> <ePresentation>Direct value, X</ePresentation> </Property> <PhaseID> <ePhase>Liquid</ePhase> </PhaseID> <PhaseID> <ePhase>Crystal</ePhase> </PhaseID> <Variable> <nVarNumber>1</nVarNumber> <VariableID> <VariableType> <ePressure>Pressure, kPa</ePressure> </VariableType> </VariableID> </Variable> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>101.3</nVarValue> <nVarDigits>4</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>313.65</nPropValue> <nPropDigits>5</nPropDigits> </PropertyValue> </NumValues> </PureOrMixtureData> <PureOrMixtureData> <Component> <RegNum> <nOrgNum>3</nOrgNum> </RegNum> <nSampleNm>1</nSampleNm> </Component> <eExpPurpose>Principal objective of the work</eExpPurpose> <sCompiler>RDC</sCompiler> <sContributor>TRC</sContributor> <dateDateAdded>11/14/2003</dateDateAdded> <Property> <nPropNumber>1</nPropNumber> <Property-MethodID> <PropertyGroup> <PhaseTransition> <ePropName>Solid-liquid equilibrium temperature, K</ePropName> <eMethodName>Visual observation</eMethodName> </PhaseTransition> </PropertyGroup> </Property-MethodID> <PropPhaseID> <ePropPhase>Liquid</ePropPhase> </PropPhaseID> <ePresentation>Direct value, X</ePresentation> </Property> <PhaseID> <ePhase>Liquid</ePhase> </PhaseID> <PhaseID> <ePhase>Crystal</ePhase> </PhaseID> <Variable> <nVarNumber>1</nVarNumber> <VariableID> <VariableType> <ePressure>Pressure, kPa</ePressure> </VariableType> </VariableID> </Variable> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>101.3</nVarValue> <nVarDigits>4</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>298.3</nPropValue> <nPropDigits>5</nPropDigits> </PropertyValue> </NumValues> </PureOrMixtureData> <PureOrMixtureData> <Component> <RegNum> <nOrgNum>4</nOrgNum> </RegNum> <nSampleNm>1</nSampleNm> </Component> <eExpPurpose>Principal objective of the work</eExpPurpose> <sCompiler>RDC</sCompiler> <sContributor>TRC</sContributor> <dateDateAdded>11/14/2003</dateDateAdded> <Property> <nPropNumber>1</nPropNumber> <Property-MethodID> <PropertyGroup> <PhaseTransition> <ePropName>Solid-liquid equilibrium temperature, K</ePropName> <eMethodName>Visual observation</eMethodName> </PhaseTransition> </PropertyGroup> </Property-MethodID> <PropPhaseID> <ePropPhase>Liquid</ePropPhase> </PropPhaseID> <ePresentation>Direct value, X</ePresentation> </Property> <PhaseID> <ePhase>Liquid</ePhase> </PhaseID> <PhaseID> <ePhase>Crystal</ePhase> </PhaseID> <Variable> <nVarNumber>1</nVarNumber> <VariableID> <VariableType> <ePressure>Pressure, kPa</ePressure> </VariableType> </VariableID> </Variable> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>101.3</nVarValue> <nVarDigits>4</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>175.49</nPropValue> <nPropDigits>5</nPropDigits> </PropertyValue> </NumValues> </PureOrMixtureData> <PureOrMixtureData> <Component> <RegNum> <nOrgNum>5</nOrgNum> </RegNum> <nSampleNm>1</nSampleNm> </Component> <eExpPurpose>Principal objective of the work</eExpPurpose> <sCompiler>RDC</sCompiler> <sContributor>TRC</sContributor> <dateDateAdded>11/14/2003</dateDateAdded> <Property> <nPropNumber>1</nPropNumber> <Property-MethodID> <PropertyGroup> <PhaseTransition> <ePropName>Solid-liquid equilibrium temperature, K</ePropName> <eMethodName>Visual observation</eMethodName> </PhaseTransition> </PropertyGroup> </Property-MethodID> <PropPhaseID> <ePropPhase>Liquid</ePropPhase> </PropPhaseID> <ePresentation>Direct value, X</ePresentation> </Property> <PhaseID> <ePhase>Liquid</ePhase> </PhaseID> <PhaseID> <ePhase>Crystal</ePhase> </PhaseID> <Variable> <nVarNumber>1</nVarNumber> <VariableID> <VariableType> <ePressure>Pressure, kPa</ePressure> </VariableType> </VariableID> </Variable> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>101.3</nVarValue> <nVarDigits>4</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>159.12</nPropValue> <nPropDigits>5</nPropDigits> </PropertyValue> </NumValues> </PureOrMixtureData> <PureOrMixtureData> <Component> <RegNum> <nOrgNum>6</nOrgNum> </RegNum> <nSampleNm>1</nSampleNm> </Component> <eExpPurpose>Principal objective of the work</eExpPurpose> <sCompiler>RDC</sCompiler> <sContributor>TRC</sContributor> <dateDateAdded>11/14/2003</dateDateAdded> <Property> <nPropNumber>1</nPropNumber> <Property-MethodID> <PropertyGroup> <PhaseTransition> <ePropName>Solid-liquid equilibrium temperature, K</ePropName> <eMethodName>Visual observation</eMethodName> </PhaseTransition> </PropertyGroup> </Property-MethodID> <PropPhaseID> <ePropPhase>Liquid</ePropPhase> </PropPhaseID> <ePresentation>Direct value, X</ePresentation> </Property> <PhaseID> <ePhase>Liquid</ePhase> </PhaseID> <PhaseID> <ePhase>Crystal</ePhase> </PhaseID> <Variable> <nVarNumber>1</nVarNumber> <VariableID> <VariableType> <ePressure>Pressure, kPa</ePressure> </VariableType> </VariableID> </Variable> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>101.3</nVarValue> <nVarDigits>4</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>147.09</nPropValue> <nPropDigits>5</nPropDigits> </PropertyValue> </NumValues> </PureOrMixtureData> <PureOrMixtureData> <Component> <RegNum> <nOrgNum>7</nOrgNum> </RegNum> <nSampleNm>1</nSampleNm> </Component> <eExpPurpose>Principal objective of the work</eExpPurpose> <sCompiler>RDC</sCompiler> <sContributor>TRC</sContributor> <dateDateAdded>11/14/2003</dateDateAdded> <Property> <nPropNumber>1</nPropNumber> <Property-MethodID> <PropertyGroup> <PhaseTransition> <ePropName>Solid-liquid equilibrium temperature, K</ePropName> <eMethodName>Visual observation</eMethodName> </PhaseTransition> </PropertyGroup> </Property-MethodID> <PropPhaseID> <ePropPhase>Liquid</ePropPhase> </PropPhaseID> <ePresentation>Direct value, X</ePresentation> </Property> <PhaseID> <ePhase>Liquid</ePhase> </PhaseID> <PhaseID> <ePhase>Crystal</ePhase> </PhaseID> <Variable> <nVarNumber>1</nVarNumber> <VariableID> <VariableType> <ePressure>Pressure, kPa</ePressure> </VariableType> </VariableID> </Variable> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>101.3</nVarValue> <nVarDigits>4</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>184.43</nPropValue> <nPropDigits>5</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>JCE</sCompiler> <sContributor>JCE</sContributor> <dateDateAdded>7/27/2003</dateDateAdded> <Property> <nPropNumber>1</nPropNumber> <Property-MethodID> <PropertyGroup> <CompositionAtPhaseEquilibrium> <ePropName>Eutectic composition: mole fraction</ePropName> <eMethodName>Derived from phase diagram analysis</eMethodName> </CompositionAtPhaseEquilibrium> </PropertyGroup> <RegNum> <nOrgNum>2</nOrgNum> </RegNum> </Property-MethodID> <PropPhaseID> <ePropPhase>Crystal</ePropPhase> </PropPhaseID> <ePresentation>Direct value, X</ePresentation> </Property> <PhaseID> <ePhase>Crystal</ePhase> <RegNum> <nOrgNum>1</nOrgNum> </RegNum> </PhaseID> <PhaseID> <ePhase>Crystal of intercomponent compound 1</ePhase> </PhaseID> <PhaseID> <ePhase>Liquid</ePhase> </PhaseID> <PhaseID> <ePhase>Air at 1 atmosphere</ePhase> </PhaseID> <Constraint> <ConstraintID> <ConstraintType> <ePressure>Pressure, kPa</ePressure> </ConstraintType> </ConstraintID> <ConstraintPhaseID> <eConstraintPhase>Crystal</eConstraintPhase> </ConstraintPhaseID> <nConstraintValue>101.325</nConstraintValue> <nConstrDigits>6</nConstrDigits> </Constraint> <NumValues> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>.28</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>JCE</sCompiler> <sContributor>JCE</sContributor> <dateDateAdded>7/27/2003</dateDateAdded> <Property> <nPropNumber>1</nPropNumber> <Property-MethodID> <PropertyGroup> <PhaseTransition> <ePropName>Eutectic temperature, K</ePropName> <eMethodName>Derived from phase diagram analysis</eMethodName> </PhaseTransition> </PropertyGroup> </Property-MethodID> <PropPhaseID> <ePropPhase>Crystal</ePropPhase> </PropPhaseID> <ePresentation>Direct value, X</ePresentation> </Property> <PhaseID> <ePhase>Crystal</ePhase> <RegNum> <nOrgNum>1</nOrgNum> </RegNum> </PhaseID> <PhaseID> <ePhase>Crystal of intercomponent compound 1</ePhase> </PhaseID> <PhaseID> <ePhase>Liquid</ePhase> </PhaseID> <PhaseID> <ePhase>Air at 1 atmosphere</ePhase> </PhaseID> <Constraint> <ConstraintID> <ConstraintType> <ePressure>Pressure, kPa</ePressure> </ConstraintType> </ConstraintID> <ConstraintPhaseID> <eConstraintPhase>Crystal</eConstraintPhase> </ConstraintPhaseID> <nConstraintValue>101.325</nConstraintValue> <nConstrDigits>6</nConstrDigits> </Constraint> <NumValues> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>256</nPropValue> <nPropDigits>4</nPropDigits> </PropertyValue> </NumValues> </PureOrMixtureData> <PureOrMixtureData> <Component> <RegNum> <nOrgNum>2</nOrgNum> </RegNum> <nSampleNm>1</nSampleNm> </Component> <Component> <RegNum> <nOrgNum>1</nOrgNum> </RegNum> <nSampleNm>1</nSampleNm> </Component> <eExpPurpose>Principal objective of the work</eExpPurpose> <sCompiler>JCE</sCompiler> <sContributor>JCE</sContributor> <dateDateAdded>7/27/2003</dateDateAdded> <Property> <nPropNumber>1</nPropNumber> <Property-MethodID> <PropertyGroup> <CompositionAtPhaseEquilibrium> <ePropName>Eutectic composition: mole fraction</ePropName> <eMethodName>Derived from phase diagram analysis</eMethodName> </CompositionAtPhaseEquilibrium> </PropertyGroup> <RegNum> <nOrgNum>2</nOrgNum> </RegNum> </Property-MethodID> <PropPhaseID> <ePropPhase>Crystal of intercomponent compound 1</ePropPhase> </PropPhaseID> <ePresentation>Direct value, X</ePresentation> </Property> <PhaseID> <ePhase>Crystal of intercomponent compound 1</ePhase> </PhaseID> <PhaseID> <ePhase>Crystal</ePhase> <RegNum> <nOrgNum>2</nOrgNum> </RegNum> </PhaseID> <PhaseID> <ePhase>Liquid</ePhase> </PhaseID> <PhaseID> <ePhase>Air at 1 atmosphere</ePhase> </PhaseID> <Constraint> <ConstraintID> <ConstraintType> <ePressure>Pressure, kPa</ePressure> </ConstraintType> </ConstraintID> <ConstraintPhaseID> <eConstraintPhase>Crystal of intercomponent compound 1</eConstraintPhase> </ConstraintPhaseID> <nConstraintValue>101.325</nConstraintValue> <nConstrDigits>6</nConstrDigits> </Constraint> <NumValues> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>.625</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>JCE</sCompiler> <sContributor>JCE</sContributor> <dateDateAdded>7/27/2003</dateDateAdded> <Property> <nPropNumber>1</nPropNumber> <Property-MethodID> <PropertyGroup> <PhaseTransition> <ePropName>Eutectic temperature, K</ePropName> <eMethodName>Derived from phase diagram analysis</eMethodName> </PhaseTransition> </PropertyGroup> </Property-MethodID> <PropPhaseID> <ePropPhase>Crystal of intercomponent compound 1</ePropPhase> </PropPhaseID> <ePresentation>Direct value, X</ePresentation> </Property> <PhaseID> <ePhase>Crystal of intercomponent compound 1</ePhase> </PhaseID> <PhaseID> <ePhase>Crystal</ePhase> <RegNum> <nOrgNum>2</nOrgNum> </RegNum> </PhaseID> <PhaseID> <ePhase>Liquid</ePhase> </PhaseID> <PhaseID> <ePhase>Air at 1 atmosphere</ePhase> </PhaseID> <Constraint> <ConstraintID> <ConstraintType> <ePressure>Pressure, kPa</ePressure> </ConstraintType> </ConstraintID> <ConstraintPhaseID> <eConstraintPhase>Crystal of intercomponent compound 1</eConstraintPhase> </ConstraintPhaseID> <nConstraintValue>101.325</nConstraintValue> <nConstrDigits>6</nConstrDigits> </Constraint> <NumValues> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>244.6</nPropValue> <nPropDigits>4</nPropDigits> </PropertyValue> </NumValues> </PureOrMixtureData> <PureOrMixtureData> <Component> <RegNum> <nOrgNum>2</nOrgNum> </RegNum> <nSampleNm>1</nSampleNm> </Component> <Component> <RegNum> <nOrgNum>1</nOrgNum> </RegNum> <nSampleNm>1</nSampleNm> </Component> <eExpPurpose>Principal objective of the work</eExpPurpose> <sCompiler>JCE</sCompiler> <sContributor>JCE</sContributor> <dateDateAdded>7/27/2003</dateDateAdded> <Property> <nPropNumber>1</nPropNumber> <Property-MethodID> <PropertyGroup> <PhaseTransition> <ePropName>Solid-liquid equilibrium temperature, K</ePropName> <eMethodName>Visual observation</eMethodName> </PhaseTransition> </PropertyGroup> </Property-MethodID> <PropPhaseID> <ePropPhase>Liquid</ePropPhase> </PropPhaseID> <ePresentation>Direct value, X</ePresentation> </Property> <PhaseID> <ePhase>Liquid</ePhase> </PhaseID> <PhaseID> <ePhase>Crystal</ePhase> <RegNum> <nOrgNum>2</nOrgNum> </RegNum> </PhaseID> <Constraint> <ConstraintID> <ConstraintType> <ePressure>Pressure, kPa</ePressure> </ConstraintType> </ConstraintID> <nConstraintValue>101.3</nConstraintValue> <nConstrDigits>4</nConstrDigits> </Constraint> <Variable> <nVarNumber>1</nVarNumber> <VariableID> <VariableType> <eComponentComposition>Mole fraction</eComponentComposition> </VariableType> <RegNum> <nOrgNum>2</nOrgNum> </RegNum> </VariableID> <VarPhaseID> <eVarPhase>Liquid</eVarPhase> </VarPhaseID> </Variable> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.6504</nVarValue> <nVarDigits>4</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>252.51</nPropValue> <nPropDigits>5</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.7003</nVarValue> <nVarDigits>4</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>266.39</nPropValue> <nPropDigits>5</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.7496</nVarValue> <nVarDigits>4</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>278.35</nPropValue> <nPropDigits>5</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.7996</nVarValue> <nVarDigits>4</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>288.63</nPropValue> <nPropDigits>5</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.8497</nVarValue> <nVarDigits>4</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>297.12</nPropValue> <nPropDigits>5</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.8999</nVarValue> <nVarDigits>4</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>304.15</nPropValue> <nPropDigits>5</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.9499</nVarValue> <nVarDigits>4</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>309.4</nPropValue> <nPropDigits>5</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>1</nVarValue> <nVarDigits>5</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>313.65</nPropValue> <nPropDigits>5</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>JCE</sCompiler> <sContributor>JCE</sContributor> <dateDateAdded>8/4/2003</dateDateAdded> <Property> <nPropNumber>1</nPropNumber> <Property-MethodID> <PropertyGroup> <PhaseTransition> <ePropName>Solid-liquid equilibrium temperature, K</ePropName> <eMethodName>Visual observation</eMethodName> </PhaseTransition> </PropertyGroup> </Property-MethodID> <PropPhaseID> <ePropPhase>Liquid</ePropPhase> </PropPhaseID> <ePresentation>Direct value, X</ePresentation> </Property> <PhaseID> <ePhase>Liquid</ePhase> </PhaseID> <PhaseID> <ePhase>Crystal of intercomponent compound 1</ePhase> </PhaseID> <Constraint> <ConstraintID> <ConstraintType> <ePressure>Pressure, kPa</ePressure> </ConstraintType> </ConstraintID> <nConstraintValue>101.3</nConstraintValue> <nConstrDigits>4</nConstrDigits> </Constraint> <Variable> <nVarNumber>1</nVarNumber> <VariableID> <VariableType> <eComponentComposition>Mole fraction</eComponentComposition> </VariableType> <RegNum> <nOrgNum>2</nOrgNum> </RegNum> </VariableID> <VarPhaseID> <eVarPhase>Liquid</eVarPhase> </VarPhaseID> </Variable> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.3002</nVarValue> <nVarDigits>4</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>258.01</nPropValue> <nPropDigits>5</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.3505</nVarValue> <nVarDigits>4</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>262.71</nPropValue> <nPropDigits>5</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.3996</nVarValue> <nVarDigits>4</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>266.83</nPropValue> <nPropDigits>5</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.4498</nVarValue> <nVarDigits>4</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>269.73</nPropValue> <nPropDigits>5</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.5002</nVarValue> <nVarDigits>4</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>270.44</nPropValue> <nPropDigits>5</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.5499</nVarValue> <nVarDigits>4</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>266.49</nPropValue> <nPropDigits>5</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.5998</nVarValue> <nVarDigits>4</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>254.98</nPropValue> <nPropDigits>5</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>JCE</sCompiler> <sContributor>JCE</sContributor> <dateDateAdded>8/4/2003</dateDateAdded> <Property> <nPropNumber>1</nPropNumber> <Property-MethodID> <PropertyGroup> <PhaseTransition> <ePropName>Solid-liquid equilibrium temperature, K</ePropName> <eMethodName>Visual observation</eMethodName> </PhaseTransition> </PropertyGroup> </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>101.3</nConstraintValue> <nConstrDigits>4</nConstrDigits> </Constraint> <Variable> <nVarNumber>1</nVarNumber> <VariableID> <VariableType> <eComponentComposition>Mole fraction</eComponentComposition> </VariableType> <RegNum> <nOrgNum>2</nOrgNum> </RegNum> </VariableID> <VarPhaseID> <eVarPhase>Liquid</eVarPhase> </VarPhaseID> </Variable> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>0</nVarValue> <nVarDigits>0</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>274.42</nPropValue> <nPropDigits>5</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.0504</nVarValue> <nVarDigits>3</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>271.63</nPropValue> <nPropDigits>5</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.0998</nVarValue> <nVarDigits>3</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>268.68</nPropValue> <nPropDigits>5</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.1497</nVarValue> <nVarDigits>4</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>265.49</nPropValue> <nPropDigits>5</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.2002</nVarValue> <nVarDigits>4</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>262.13</nPropValue> <nPropDigits>5</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.2497</nVarValue> <nVarDigits>4</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>258.37</nPropValue> <nPropDigits>5</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>JCE</sCompiler> <sContributor>JCE</sContributor> <dateDateAdded>7/27/2003</dateDateAdded> <Property> <nPropNumber>1</nPropNumber> <Property-MethodID> <PropertyGroup> <CompositionAtPhaseEquilibrium> <ePropName>Eutectic composition: mole fraction</ePropName> <eMethodName>Derived from phase diagram analysis</eMethodName> </CompositionAtPhaseEquilibrium> </PropertyGroup> <RegNum> <nOrgNum>3</nOrgNum> </RegNum> </Property-MethodID> <PropPhaseID> <ePropPhase>Crystal</ePropPhase> </PropPhaseID> <ePresentation>Direct value, X</ePresentation> </Property> <PhaseID> <ePhase>Crystal</ePhase> <RegNum> <nOrgNum>1</nOrgNum> </RegNum> </PhaseID> <PhaseID> <ePhase>Crystal of intercomponent compound 1</ePhase> </PhaseID> <PhaseID> <ePhase>Liquid</ePhase> </PhaseID> <PhaseID> <ePhase>Air at 1 atmosphere</ePhase> </PhaseID> <Constraint> <ConstraintID> <ConstraintType> <ePressure>Pressure, kPa</ePressure> </ConstraintType> </ConstraintID> <ConstraintPhaseID> <eConstraintPhase>Crystal</eConstraintPhase> </ConstraintPhaseID> <nConstraintValue>101.325</nConstraintValue> <nConstrDigits>6</nConstrDigits> </Constraint> <NumValues> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>.442</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>JCE</sCompiler> <sContributor>JCE</sContributor> <dateDateAdded>7/27/2003</dateDateAdded> <Property> <nPropNumber>1</nPropNumber> <Property-MethodID> <PropertyGroup> <PhaseTransition> <ePropName>Eutectic temperature, K</ePropName> <eMethodName>Derived from phase diagram analysis</eMethodName> </PhaseTransition> </PropertyGroup> </Property-MethodID> <PropPhaseID> <ePropPhase>Crystal</ePropPhase> </PropPhaseID> <ePresentation>Direct value, X</ePresentation> </Property> <PhaseID> <ePhase>Crystal</ePhase> <RegNum> <nOrgNum>1</nOrgNum> </RegNum> </PhaseID> <PhaseID> <ePhase>Crystal of intercomponent compound 1</ePhase> </PhaseID> <PhaseID> <ePhase>Liquid</ePhase> </PhaseID> <PhaseID> <ePhase>Air at 1 atmosphere</ePhase> </PhaseID> <Constraint> <ConstraintID> <ConstraintType> <ePressure>Pressure, kPa</ePressure> </ConstraintType> </ConstraintID> <ConstraintPhaseID> <eConstraintPhase>Crystal</eConstraintPhase> </ConstraintPhaseID> <nConstraintValue>101.325</nConstraintValue> <nConstrDigits>6</nConstrDigits> </Constraint> <NumValues> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>249</nPropValue> <nPropDigits>4</nPropDigits> </PropertyValue> </NumValues> </PureOrMixtureData> <PureOrMixtureData> <Component> <RegNum> <nOrgNum>3</nOrgNum> </RegNum> <nSampleNm>1</nSampleNm> </Component> <Component> <RegNum> <nOrgNum>1</nOrgNum> </RegNum> <nSampleNm>1</nSampleNm> </Component> <eExpPurpose>Principal objective of the work</eExpPurpose> <sCompiler>JCE</sCompiler> <sContributor>JCE</sContributor> <dateDateAdded>7/27/2003</dateDateAdded> <Property> <nPropNumber>1</nPropNumber> <Property-MethodID> <PropertyGroup> <CompositionAtPhaseEquilibrium> <ePropName>Eutectic composition: mole fraction</ePropName> <eMethodName>Derived from phase diagram analysis</eMethodName> </CompositionAtPhaseEquilibrium> </PropertyGroup> <RegNum> <nOrgNum>3</nOrgNum> </RegNum> </Property-MethodID> <PropPhaseID> <ePropPhase>Crystal of intercomponent compound 1</ePropPhase> </PropPhaseID> <ePresentation>Direct value, X</ePresentation> </Property> <PhaseID> <ePhase>Crystal of intercomponent compound 1</ePhase> </PhaseID> <PhaseID> <ePhase>Crystal</ePhase> <RegNum> <nOrgNum>3</nOrgNum> </RegNum> </PhaseID> <PhaseID> <ePhase>Liquid</ePhase> </PhaseID> <PhaseID> <ePhase>Air at 1 atmosphere</ePhase> </PhaseID> <Constraint> <ConstraintID> <ConstraintType> <ePressure>Pressure, kPa</ePressure> </ConstraintType> </ConstraintID> <ConstraintPhaseID> <eConstraintPhase>Crystal of intercomponent compound 1</eConstraintPhase> </ConstraintPhaseID> <nConstraintValue>101.325</nConstraintValue> <nConstrDigits>6</nConstrDigits> </Constraint> <NumValues> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>.756</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>JCE</sCompiler> <sContributor>JCE</sContributor> <dateDateAdded>7/27/2003</dateDateAdded> <Property> <nPropNumber>1</nPropNumber> <Property-MethodID> <PropertyGroup> <PhaseTransition> <ePropName>Eutectic temperature, K</ePropName> <eMethodName>Derived from phase diagram analysis</eMethodName> </PhaseTransition> </PropertyGroup> </Property-MethodID> <PropPhaseID> <ePropPhase>Crystal of intercomponent compound 1</ePropPhase> </PropPhaseID> <ePresentation>Direct value, X</ePresentation> </Property> <PhaseID> <ePhase>Crystal of intercomponent compound 1</ePhase> </PhaseID> <PhaseID> <ePhase>Crystal</ePhase> <RegNum> <nOrgNum>3</nOrgNum> </RegNum> </PhaseID> <PhaseID> <ePhase>Liquid</ePhase> </PhaseID> <PhaseID> <ePhase>Air at 1 atmosphere</ePhase> </PhaseID> <Constraint> <ConstraintID> <ConstraintType> <ePressure>Pressure, kPa</ePressure> </ConstraintType> </ConstraintID> <ConstraintPhaseID> <eConstraintPhase>Crystal of intercomponent compound 1</eConstraintPhase> </ConstraintPhaseID> <nConstraintValue>101.325</nConstraintValue> <nConstrDigits>6</nConstrDigits> </Constraint> <NumValues> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>222.2</nPropValue> <nPropDigits>4</nPropDigits> </PropertyValue> </NumValues> </PureOrMixtureData> <PureOrMixtureData> <Component> <RegNum> <nOrgNum>3</nOrgNum> </RegNum> <nSampleNm>1</nSampleNm> </Component> <Component> <RegNum> <nOrgNum>1</nOrgNum> </RegNum> <nSampleNm>1</nSampleNm> </Component> <eExpPurpose>Principal objective of the work</eExpPurpose> <sCompiler>JCE</sCompiler> <sContributor>JCE</sContributor> <dateDateAdded>7/27/2003</dateDateAdded> <Property> <nPropNumber>1</nPropNumber> <Property-MethodID> <PropertyGroup> <PhaseTransition> <ePropName>Solid-liquid equilibrium temperature, K</ePropName> <eMethodName>Visual observation</eMethodName> </PhaseTransition> </PropertyGroup> </Property-MethodID> <PropPhaseID> <ePropPhase>Liquid</ePropPhase> </PropPhaseID> <ePresentation>Direct value, X</ePresentation> </Property> <PhaseID> <ePhase>Liquid</ePhase> </PhaseID> <PhaseID> <ePhase>Crystal</ePhase> <RegNum> <nOrgNum>3</nOrgNum> </RegNum> </PhaseID> <Constraint> <ConstraintID> <ConstraintType> <ePressure>Pressure, kPa</ePressure> </ConstraintType> </ConstraintID> <nConstraintValue>101.3</nConstraintValue> <nConstrDigits>4</nConstrDigits> </Constraint> <Variable> <nVarNumber>1</nVarNumber> <VariableID> <VariableType> <eComponentComposition>Mole fraction</eComponentComposition> </VariableType> <RegNum> <nOrgNum>3</nOrgNum> </RegNum> </VariableID> <VarPhaseID> <eVarPhase>Liquid</eVarPhase> </VarPhaseID> </Variable> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.7675</nVarValue> <nVarDigits>4</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>227.05</nPropValue> <nPropDigits>5</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.7995</nVarValue> <nVarDigits>4</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>239.76</nPropValue> <nPropDigits>5</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.8497</nVarValue> <nVarDigits>4</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>257.71</nPropValue> <nPropDigits>5</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.9001</nVarValue> <nVarDigits>4</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>273.18</nPropValue> <nPropDigits>5</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.9499</nVarValue> <nVarDigits>4</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>286.34</nPropValue> <nPropDigits>5</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>1</nVarValue> <nVarDigits>5</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>298.3</nPropValue> <nPropDigits>5</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>JCE</sCompiler> <sContributor>JCE</sContributor> <dateDateAdded>8/4/2003</dateDateAdded> <Property> <nPropNumber>1</nPropNumber> <Property-MethodID> <PropertyGroup> <PhaseTransition> <ePropName>Solid-liquid equilibrium temperature, K</ePropName> <eMethodName>Visual observation</eMethodName> </PhaseTransition> </PropertyGroup> </Property-MethodID> <PropPhaseID> <ePropPhase>Liquid</ePropPhase> </PropPhaseID> <ePresentation>Direct value, X</ePresentation> </Property> <PhaseID> <ePhase>Liquid</ePhase> </PhaseID> <PhaseID> <ePhase>Crystal of intercomponent compound 1</ePhase> </PhaseID> <Constraint> <ConstraintID> <ConstraintType> <ePressure>Pressure, kPa</ePressure> </ConstraintType> </ConstraintID> <nConstraintValue>101.3</nConstraintValue> <nConstrDigits>4</nConstrDigits> </Constraint> <Variable> <nVarNumber>1</nVarNumber> <VariableID> <VariableType> <eComponentComposition>Mole fraction</eComponentComposition> </VariableType> <RegNum> <nOrgNum>3</nOrgNum> </RegNum> </VariableID> <VarPhaseID> <eVarPhase>Liquid</eVarPhase> </VarPhaseID> </Variable> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.4496</nVarValue> <nVarDigits>4</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>252</nPropValue> <nPropDigits>5</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.47</nVarValue> <nVarDigits>4</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>255.5</nPropValue> <nPropDigits>5</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.4999</nVarValue> <nVarDigits>4</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>257.33</nPropValue> <nPropDigits>5</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.54</nVarValue> <nVarDigits>4</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>255.5</nPropValue> <nPropDigits>5</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.5503</nVarValue> <nVarDigits>4</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>254.68</nPropValue> <nPropDigits>5</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.6005</nVarValue> <nVarDigits>4</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>248.98</nPropValue> <nPropDigits>5</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.6502</nVarValue> <nVarDigits>4</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>241.67</nPropValue> <nPropDigits>5</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.7</nVarValue> <nVarDigits>4</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>232.95</nPropValue> <nPropDigits>5</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.749</nVarValue> <nVarDigits>4</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>223.47</nPropValue> <nPropDigits>5</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>JCE</sCompiler> <sContributor>JCE</sContributor> <dateDateAdded>8/4/2003</dateDateAdded> <Property> <nPropNumber>1</nPropNumber> <Property-MethodID> <PropertyGroup> <PhaseTransition> <ePropName>Solid-liquid equilibrium temperature, K</ePropName> <eMethodName>Visual observation</eMethodName> </PhaseTransition> </PropertyGroup> </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>101.3</nConstraintValue> <nConstrDigits>4</nConstrDigits> </Constraint> <Variable> <nVarNumber>1</nVarNumber> <VariableID> <VariableType> <eComponentComposition>Mole fraction</eComponentComposition> </VariableType> <RegNum> <nOrgNum>3</nOrgNum> </RegNum> </VariableID> <VarPhaseID> <eVarPhase>Liquid</eVarPhase> </VarPhaseID> </Variable> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>0</nVarValue> <nVarDigits>0</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>274.42</nPropValue> <nPropDigits>5</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.0504</nVarValue> <nVarDigits>3</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>272.73</nPropValue> <nPropDigits>5</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.1002</nVarValue> <nVarDigits>4</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>271.07</nPropValue> <nPropDigits>5</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.1507</nVarValue> <nVarDigits>4</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>269.11</nPropValue> <nPropDigits>5</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.2002</nVarValue> <nVarDigits>4</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>266.71</nPropValue> <nPropDigits>5</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.2503</nVarValue> <nVarDigits>4</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>264.06</nPropValue> <nPropDigits>5</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.3024</nVarValue> <nVarDigits>4</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>260.78</nPropValue> <nPropDigits>5</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.3498</nVarValue> <nVarDigits>4</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>257.45</nPropValue> <nPropDigits>5</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.4003</nVarValue> <nVarDigits>4</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>253.5</nPropValue> <nPropDigits>5</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>JCE</sCompiler> <sContributor>JCE</sContributor> <dateDateAdded>7/27/2003</dateDateAdded> <Property> <nPropNumber>1</nPropNumber> <Property-MethodID> <PropertyGroup> <PhaseTransition> <ePropName>Eutectic temperature, K</ePropName> <eMethodName>Derived from phase diagram analysis</eMethodName> </PhaseTransition> </PropertyGroup> </Property-MethodID> <PropPhaseID> <ePropPhase>Crystal</ePropPhase> </PropPhaseID> <ePresentation>Direct value, X</ePresentation> </Property> <PhaseID> <ePhase>Crystal</ePhase> <RegNum> <nOrgNum>4</nOrgNum> </RegNum> </PhaseID> <PhaseID> <ePhase>Crystal</ePhase> <RegNum> <nOrgNum>1</nOrgNum> </RegNum> </PhaseID> <PhaseID> <ePhase>Liquid</ePhase> </PhaseID> <PhaseID> <ePhase>Air at 1 atmosphere</ePhase> </PhaseID> <Constraint> <ConstraintID> <ConstraintType> <ePressure>Pressure, kPa</ePressure> </ConstraintType> </ConstraintID> <ConstraintPhaseID> <eConstraintPhase>Crystal</eConstraintPhase> </ConstraintPhaseID> <nConstraintValue>101.325</nConstraintValue> <nConstrDigits>6</nConstrDigits> </Constraint> <NumValues> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>175.5</nPropValue> <nPropDigits>4</nPropDigits> </PropertyValue> </NumValues> </PureOrMixtureData> <PureOrMixtureData> <Component> <RegNum> <nOrgNum>4</nOrgNum> </RegNum> <nSampleNm>1</nSampleNm> </Component> <Component> <RegNum> <nOrgNum>1</nOrgNum> </RegNum> <nSampleNm>1</nSampleNm> </Component> <eExpPurpose>Principal objective of the work</eExpPurpose> <sCompiler>JCE</sCompiler> <sContributor>JCE</sContributor> <dateDateAdded>7/27/2003</dateDateAdded> <Property> <nPropNumber>1</nPropNumber> <Property-MethodID> <PropertyGroup> <CompositionAtPhaseEquilibrium> <ePropName>Eutectic composition: mole fraction</ePropName> <eMethodName>Derived from phase diagram analysis</eMethodName> </CompositionAtPhaseEquilibrium> </PropertyGroup> <RegNum> <nOrgNum>4</nOrgNum> </RegNum> </Property-MethodID> <PropPhaseID> <ePropPhase>Crystal</ePropPhase> </PropPhaseID> <ePresentation>Direct value, X</ePresentation> </Property> <PhaseID> <ePhase>Crystal</ePhase> <RegNum> <nOrgNum>4</nOrgNum> </RegNum> </PhaseID> <PhaseID> <ePhase>Crystal</ePhase> <RegNum> <nOrgNum>1</nOrgNum> </RegNum> </PhaseID> <PhaseID> <ePhase>Liquid</ePhase> </PhaseID> <PhaseID> <ePhase>Air at 1 atmosphere</ePhase> </PhaseID> <Constraint> <ConstraintID> <ConstraintType> <ePressure>Pressure, kPa</ePressure> </ConstraintType> </ConstraintID> <ConstraintPhaseID> <eConstraintPhase>Crystal</eConstraintPhase> </ConstraintPhaseID> <nConstraintValue>101.325</nConstraintValue> <nConstrDigits>6</nConstrDigits> </Constraint> <NumValues> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>.995</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>JCE</sCompiler> <sContributor>JCE</sContributor> <dateDateAdded>7/27/2003</dateDateAdded> <Property> <nPropNumber>1</nPropNumber> <Property-MethodID> <PropertyGroup> <PhaseTransition> <ePropName>Solid-liquid equilibrium temperature, K</ePropName> <eMethodName>Visual observation</eMethodName> </PhaseTransition> </PropertyGroup> </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>101.3</nConstraintValue> <nConstrDigits>4</nConstrDigits> </Constraint> <Variable> <nVarNumber>1</nVarNumber> <VariableID> <VariableType> <eComponentComposition>Mole fraction</eComponentComposition> </VariableType> <RegNum> <nOrgNum>4</nOrgNum> </RegNum> </VariableID> <VarPhaseID> <eVarPhase>Liquid</eVarPhase> </VarPhaseID> </Variable> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>0</nVarValue> <nVarDigits>0</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>274.42</nPropValue> <nPropDigits>5</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.0512</nVarValue> <nVarDigits>3</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>271.9</nPropValue> <nPropDigits>5</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.105</nVarValue> <nVarDigits>4</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>270.17</nPropValue> <nPropDigits>5</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.1512</nVarValue> <nVarDigits>4</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>268.98</nPropValue> <nPropDigits>5</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.2063</nVarValue> <nVarDigits>4</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>267.59</nPropValue> <nPropDigits>5</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.2532</nVarValue> <nVarDigits>4</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>266.28</nPropValue> <nPropDigits>5</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.3172</nVarValue> <nVarDigits>4</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>264.15</nPropValue> <nPropDigits>5</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.3568</nVarValue> <nVarDigits>4</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>262.76</nPropValue> <nPropDigits>5</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.4026</nVarValue> <nVarDigits>4</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>261.03</nPropValue> <nPropDigits>5</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.4519</nVarValue> <nVarDigits>4</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>259.32</nPropValue> <nPropDigits>5</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.5017</nVarValue> <nVarDigits>4</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>257.74</nPropValue> <nPropDigits>5</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.5515</nVarValue> <nVarDigits>4</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>256.42</nPropValue> <nPropDigits>5</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.6017</nVarValue> <nVarDigits>4</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>255.29</nPropValue> <nPropDigits>5</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.6513</nVarValue> <nVarDigits>4</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>254.11</nPropValue> <nPropDigits>5</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.7004</nVarValue> <nVarDigits>4</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>252.46</nPropValue> <nPropDigits>5</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.7447</nVarValue> <nVarDigits>4</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>250.01</nPropValue> <nPropDigits>5</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.8003</nVarValue> <nVarDigits>4</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>244.59</nPropValue> <nPropDigits>5</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.8501</nVarValue> <nVarDigits>4</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>236.12</nPropValue> <nPropDigits>5</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.9</nVarValue> <nVarDigits>4</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>222.51</nPropValue> <nPropDigits>5</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.95</nVarValue> <nVarDigits>4</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>201.65</nPropValue> <nPropDigits>5</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.9701</nVarValue> <nVarDigits>4</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>190.56</nPropValue> <nPropDigits>5</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>JCE</sCompiler> <sContributor>JCE</sContributor> <dateDateAdded>8/4/2003</dateDateAdded> <Property> <nPropNumber>1</nPropNumber> <Property-MethodID> <PropertyGroup> <PhaseTransition> <ePropName>Solid-liquid equilibrium temperature, K</ePropName> <eMethodName>Visual observation</eMethodName> </PhaseTransition> </PropertyGroup> </Property-MethodID> <PropPhaseID> <ePropPhase>Liquid</ePropPhase> </PropPhaseID> <ePresentation>Direct value, X</ePresentation> </Property> <PhaseID> <ePhase>Liquid</ePhase> </PhaseID> <PhaseID> <ePhase>Crystal</ePhase> <RegNum> <nOrgNum>4</nOrgNum> </RegNum> </PhaseID> <Constraint> <ConstraintID> <ConstraintType> <ePressure>Pressure, kPa</ePressure> </ConstraintType> </ConstraintID> <nConstraintValue>101.3</nConstraintValue> <nConstrDigits>4</nConstrDigits> </Constraint> <Variable> <nVarNumber>1</nVarNumber> <VariableID> <VariableType> <eComponentComposition>Mole fraction</eComponentComposition> </VariableType> <RegNum> <nOrgNum>4</nOrgNum> </RegNum> </VariableID> <VarPhaseID> <eVarPhase>Liquid</eVarPhase> </VarPhaseID> </Variable> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>1</nVarValue> <nVarDigits>5</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>175.49</nPropValue> <nPropDigits>5</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>JCE</sCompiler> <sContributor>JCE</sContributor> <dateDateAdded>7/27/2003</dateDateAdded> <Property> <nPropNumber>1</nPropNumber> <Property-MethodID> <PropertyGroup> <PhaseTransition> <ePropName>Eutectic temperature, K</ePropName> <eMethodName>Derived from phase diagram analysis</eMethodName> </PhaseTransition> </PropertyGroup> </Property-MethodID> <PropPhaseID> <ePropPhase>Crystal</ePropPhase> </PropPhaseID> <ePresentation>Direct value, X</ePresentation> </Property> <PhaseID> <ePhase>Crystal</ePhase> <RegNum> <nOrgNum>5</nOrgNum> </RegNum> </PhaseID> <PhaseID> <ePhase>Crystal</ePhase> <RegNum> <nOrgNum>1</nOrgNum> </RegNum> </PhaseID> <PhaseID> <ePhase>Liquid</ePhase> </PhaseID> <PhaseID> <ePhase>Air at 1 atmosphere</ePhase> </PhaseID> <Constraint> <ConstraintID> <ConstraintType> <ePressure>Pressure, kPa</ePressure> </ConstraintType> </ConstraintID> <ConstraintPhaseID> <eConstraintPhase>Crystal</eConstraintPhase> </ConstraintPhaseID> <nConstraintValue>101.325</nConstraintValue> <nConstrDigits>6</nConstrDigits> </Constraint> <NumValues> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>159.1</nPropValue> <nPropDigits>4</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>JCE</sCompiler> <sContributor>JCE</sContributor> <dateDateAdded>7/27/2003</dateDateAdded> <Property> <nPropNumber>1</nPropNumber> <Property-MethodID> <PropertyGroup> <CompositionAtPhaseEquilibrium> <ePropName>Eutectic composition: mole fraction</ePropName> <eMethodName>Derived from phase diagram analysis</eMethodName> </CompositionAtPhaseEquilibrium> </PropertyGroup> <RegNum> <nOrgNum>5</nOrgNum> </RegNum> </Property-MethodID> <PropPhaseID> <ePropPhase>Crystal</ePropPhase> </PropPhaseID> <ePresentation>Direct value, X</ePresentation> </Property> <PhaseID> <ePhase>Crystal</ePhase> <RegNum> <nOrgNum>5</nOrgNum> </RegNum> </PhaseID> <PhaseID> <ePhase>Crystal</ePhase> <RegNum> <nOrgNum>1</nOrgNum> </RegNum> </PhaseID> <PhaseID> <ePhase>Liquid</ePhase> </PhaseID> <PhaseID> <ePhase>Air at 1 atmosphere</ePhase> </PhaseID> <Constraint> <ConstraintID> <ConstraintType> <ePressure>Pressure, kPa</ePressure> </ConstraintType> </ConstraintID> <ConstraintPhaseID> <eConstraintPhase>Crystal</eConstraintPhase> </ConstraintPhaseID> <nConstraintValue>101.325</nConstraintValue> <nConstrDigits>6</nConstrDigits> </Constraint> <NumValues> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>.999</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>JCE</sCompiler> <sContributor>JCE</sContributor> <dateDateAdded>7/27/2003</dateDateAdded> <Property> <nPropNumber>1</nPropNumber> <Property-MethodID> <PropertyGroup> <PhaseTransition> <ePropName>Solid-liquid equilibrium temperature, K</ePropName> <eMethodName>Visual observation</eMethodName> </PhaseTransition> </PropertyGroup> </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>101.3</nConstraintValue> <nConstrDigits>4</nConstrDigits> </Constraint> <Variable> <nVarNumber>1</nVarNumber> <VariableID> <VariableType> <eComponentComposition>Mole fraction</eComponentComposition> </VariableType> <RegNum> <nOrgNum>5</nOrgNum> </RegNum> </VariableID> <VarPhaseID> <eVarPhase>Liquid</eVarPhase> </VarPhaseID> </Variable> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>0</nVarValue> <nVarDigits>0</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>274.42</nPropValue> <nPropDigits>5</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.0507</nVarValue> <nVarDigits>3</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>272.02</nPropValue> <nPropDigits>5</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.1019</nVarValue> <nVarDigits>4</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>270.5</nPropValue> <nPropDigits>5</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.1531</nVarValue> <nVarDigits>4</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>269.3</nPropValue> <nPropDigits>5</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.2082</nVarValue> <nVarDigits>4</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>267.88</nPropValue> <nPropDigits>5</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.2601</nVarValue> <nVarDigits>4</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>266.4</nPropValue> <nPropDigits>5</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.3063</nVarValue> <nVarDigits>4</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>264.88</nPropValue> <nPropDigits>5</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.3511</nVarValue> <nVarDigits>4</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>263.27</nPropValue> <nPropDigits>5</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.4019</nVarValue> <nVarDigits>4</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>261.47</nPropValue> <nPropDigits>5</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.4541</nVarValue> <nVarDigits>4</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>259.85</nPropValue> <nPropDigits>5</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.5008</nVarValue> <nVarDigits>4</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>258.59</nPropValue> <nPropDigits>5</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.5546</nVarValue> <nVarDigits>4</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>257.72</nPropValue> <nPropDigits>5</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.5994</nVarValue> <nVarDigits>4</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>257.16</nPropValue> <nPropDigits>5</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.6509</nVarValue> <nVarDigits>4</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>256.41</nPropValue> <nPropDigits>5</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.7002</nVarValue> <nVarDigits>4</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>255.22</nPropValue> <nPropDigits>5</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.7514</nVarValue> <nVarDigits>4</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>252.43</nPropValue> <nPropDigits>5</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.8011</nVarValue> <nVarDigits>4</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>246.96</nPropValue> <nPropDigits>5</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.8502</nVarValue> <nVarDigits>4</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>237.37</nPropValue> <nPropDigits>5</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.9002</nVarValue> <nVarDigits>4</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>221.18</nPropValue> <nPropDigits>5</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.9498</nVarValue> <nVarDigits>4</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>196.26</nPropValue> <nPropDigits>5</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.9748</nVarValue> <nVarDigits>4</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>179.34</nPropValue> <nPropDigits>5</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>JCE</sCompiler> <sContributor>JCE</sContributor> <dateDateAdded>8/4/2003</dateDateAdded> <Property> <nPropNumber>1</nPropNumber> <Property-MethodID> <PropertyGroup> <PhaseTransition> <ePropName>Solid-liquid equilibrium temperature, K</ePropName> <eMethodName>Visual observation</eMethodName> </PhaseTransition> </PropertyGroup> </Property-MethodID> <PropPhaseID> <ePropPhase>Liquid</ePropPhase> </PropPhaseID> <ePresentation>Direct value, X</ePresentation> </Property> <PhaseID> <ePhase>Liquid</ePhase> </PhaseID> <PhaseID> <ePhase>Crystal</ePhase> <RegNum> <nOrgNum>5</nOrgNum> </RegNum> </PhaseID> <Constraint> <ConstraintID> <ConstraintType> <ePressure>Pressure, kPa</ePressure> </ConstraintType> </ConstraintID> <nConstraintValue>101.3</nConstraintValue> <nConstrDigits>4</nConstrDigits> </Constraint> <Variable> <nVarNumber>1</nVarNumber> <VariableID> <VariableType> <eComponentComposition>Mole fraction</eComponentComposition> </VariableType> <RegNum> <nOrgNum>5</nOrgNum> </RegNum> </VariableID> <VarPhaseID> <eVarPhase>Liquid</eVarPhase> </VarPhaseID> </Variable> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>1</nVarValue> <nVarDigits>5</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>159.12</nPropValue> <nPropDigits>5</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>JCE</sCompiler> <sContributor>JCE</sContributor> <dateDateAdded>7/27/2003</dateDateAdded> <Property> <nPropNumber>1</nPropNumber> <Property-MethodID> <PropertyGroup> <PhaseTransition> <ePropName>Eutectic temperature, K</ePropName> <eMethodName>Derived from phase diagram analysis</eMethodName> </PhaseTransition> </PropertyGroup> </Property-MethodID> <PropPhaseID> <ePropPhase>Crystal</ePropPhase> </PropPhaseID> <ePresentation>Direct value, X</ePresentation> </Property> <PhaseID> <ePhase>Crystal</ePhase> <RegNum> <nOrgNum>6</nOrgNum> </RegNum> </PhaseID> <PhaseID> <ePhase>Crystal</ePhase> <RegNum> <nOrgNum>1</nOrgNum> </RegNum> </PhaseID> <PhaseID> <ePhase>Liquid</ePhase> </PhaseID> <PhaseID> <ePhase>Air at 1 atmosphere</ePhase> </PhaseID> <Constraint> <ConstraintID> <ConstraintType> <ePressure>Pressure, kPa</ePressure> </ConstraintType> </ConstraintID> <ConstraintPhaseID> <eConstraintPhase>Crystal</eConstraintPhase> </ConstraintPhaseID> <nConstraintValue>101.325</nConstraintValue> <nConstrDigits>6</nConstrDigits> </Constraint> <NumValues> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>147.1</nPropValue> <nPropDigits>4</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>JCE</sCompiler> <sContributor>JCE</sContributor> <dateDateAdded>7/27/2003</dateDateAdded> <Property> <nPropNumber>1</nPropNumber> <Property-MethodID> <PropertyGroup> <CompositionAtPhaseEquilibrium> <ePropName>Eutectic composition: mole fraction</ePropName> <eMethodName>Derived from phase diagram analysis</eMethodName> </CompositionAtPhaseEquilibrium> </PropertyGroup> <RegNum> <nOrgNum>6</nOrgNum> </RegNum> </Property-MethodID> <PropPhaseID> <ePropPhase>Crystal</ePropPhase> </PropPhaseID> <ePresentation>Direct value, X</ePresentation> </Property> <PhaseID> <ePhase>Crystal</ePhase> <RegNum> <nOrgNum>6</nOrgNum> </RegNum> </PhaseID> <PhaseID> <ePhase>Crystal</ePhase> <RegNum> <nOrgNum>1</nOrgNum> </RegNum> </PhaseID> <PhaseID> <ePhase>Liquid</ePhase> </PhaseID> <PhaseID> <ePhase>Air at 1 atmosphere</ePhase> </PhaseID> <Constraint> <ConstraintID> <ConstraintType> <ePressure>Pressure, kPa</ePressure> </ConstraintType> </ConstraintID> <ConstraintPhaseID> <eConstraintPhase>Crystal</eConstraintPhase> </ConstraintPhaseID> <nConstraintValue>101.325</nConstraintValue> <nConstrDigits>6</nConstrDigits> </Constraint> <NumValues> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>.999</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>JCE</sCompiler> <sContributor>JCE</sContributor> <dateDateAdded>7/27/2003</dateDateAdded> <Property> <nPropNumber>1</nPropNumber> <Property-MethodID> <PropertyGroup> <PhaseTransition> <ePropName>Solid-liquid equilibrium temperature, K</ePropName> <eMethodName>Visual observation</eMethodName> </PhaseTransition> </PropertyGroup> </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>101.3</nConstraintValue> <nConstrDigits>4</nConstrDigits> </Constraint> <Variable> <nVarNumber>1</nVarNumber> <VariableID> <VariableType> <eComponentComposition>Mole fraction</eComponentComposition> </VariableType> <RegNum> <nOrgNum>6</nOrgNum> </RegNum> </VariableID> <VarPhaseID> <eVarPhase>Liquid</eVarPhase> </VarPhaseID> </Variable> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>0</nVarValue> <nVarDigits>0</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>274.42</nPropValue> <nPropDigits>5</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.0529</nVarValue> <nVarDigits>3</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>271.91</nPropValue> <nPropDigits>5</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.1017</nVarValue> <nVarDigits>4</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>270.34</nPropValue> <nPropDigits>5</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.1521</nVarValue> <nVarDigits>4</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>268.93</nPropValue> <nPropDigits>5</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.2007</nVarValue> <nVarDigits>4</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>267.56</nPropValue> <nPropDigits>5</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.251</nVarValue> <nVarDigits>4</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>266.02</nPropValue> <nPropDigits>5</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.3027</nVarValue> <nVarDigits>4</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>264.01</nPropValue> <nPropDigits>5</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.3525</nVarValue> <nVarDigits>4</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>261.88</nPropValue> <nPropDigits>5</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.4018</nVarValue> <nVarDigits>4</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>259.7</nPropValue> <nPropDigits>5</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.4516</nVarValue> <nVarDigits>4</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>257.52</nPropValue> <nPropDigits>5</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.501</nVarValue> <nVarDigits>4</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>255.6</nPropValue> <nPropDigits>5</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.5414</nVarValue> <nVarDigits>4</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>254.21</nPropValue> <nPropDigits>5</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.6009</nVarValue> <nVarDigits>4</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>252.32</nPropValue> <nPropDigits>5</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.6498</nVarValue> <nVarDigits>4</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>250.62</nPropValue> <nPropDigits>5</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.7002</nVarValue> <nVarDigits>4</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>248.11</nPropValue> <nPropDigits>5</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.7513</nVarValue> <nVarDigits>4</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>244.01</nPropValue> <nPropDigits>5</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.8001</nVarValue> <nVarDigits>4</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>237.34</nPropValue> <nPropDigits>5</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.8504</nVarValue> <nVarDigits>4</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>226.22</nPropValue> <nPropDigits>5</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.9</nVarValue> <nVarDigits>4</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>209.01</nPropValue> <nPropDigits>5</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.9501</nVarValue> <nVarDigits>4</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>182.9</nPropValue> <nPropDigits>5</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.9739</nVarValue> <nVarDigits>4</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>166.65</nPropValue> <nPropDigits>5</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>JCE</sCompiler> <sContributor>JCE</sContributor> <dateDateAdded>8/4/2003</dateDateAdded> <Property> <nPropNumber>1</nPropNumber> <Property-MethodID> <PropertyGroup> <PhaseTransition> <ePropName>Solid-liquid equilibrium temperature, K</ePropName> <eMethodName>Visual observation</eMethodName> </PhaseTransition> </PropertyGroup> </Property-MethodID> <PropPhaseID> <ePropPhase>Liquid</ePropPhase> </PropPhaseID> <ePresentation>Direct value, X</ePresentation> </Property> <PhaseID> <ePhase>Liquid</ePhase> </PhaseID> <PhaseID> <ePhase>Crystal</ePhase> <RegNum> <nOrgNum>6</nOrgNum> </RegNum> </PhaseID> <Constraint> <ConstraintID> <ConstraintType> <ePressure>Pressure, kPa</ePressure> </ConstraintType> </ConstraintID> <nConstraintValue>101.3</nConstraintValue> <nConstrDigits>4</nConstrDigits> </Constraint> <Variable> <nVarNumber>1</nVarNumber> <VariableID> <VariableType> <eComponentComposition>Mole fraction</eComponentComposition> </VariableType> <RegNum> <nOrgNum>6</nOrgNum> </RegNum> </VariableID> <VarPhaseID> <eVarPhase>Liquid</eVarPhase> </VarPhaseID> </Variable> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>1</nVarValue> <nVarDigits>5</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>147.09</nPropValue> <nPropDigits>5</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>JCE</sCompiler> <sContributor>JCE</sContributor> <dateDateAdded>7/27/2003</dateDateAdded> <Property> <nPropNumber>1</nPropNumber> <Property-MethodID> <PropertyGroup> <PhaseTransition> <ePropName>Eutectic temperature, K</ePropName> <eMethodName>Derived from phase diagram analysis</eMethodName> </PhaseTransition> </PropertyGroup> </Property-MethodID> <PropPhaseID> <ePropPhase>Crystal</ePropPhase> </PropPhaseID> <ePresentation>Direct value, X</ePresentation> </Property> <PhaseID> <ePhase>Crystal</ePhase> <RegNum> <nOrgNum>7</nOrgNum> </RegNum> </PhaseID> <PhaseID> <ePhase>Crystal</ePhase> <RegNum> <nOrgNum>1</nOrgNum> </RegNum> </PhaseID> <PhaseID> <ePhase>Liquid</ePhase> </PhaseID> <PhaseID> <ePhase>Air at 1 atmosphere</ePhase> </PhaseID> <Constraint> <ConstraintID> <ConstraintType> <ePressure>Pressure, kPa</ePressure> </ConstraintType> </ConstraintID> <ConstraintPhaseID> <eConstraintPhase>Crystal</eConstraintPhase> </ConstraintPhaseID> <nConstraintValue>101.325</nConstraintValue> <nConstrDigits>6</nConstrDigits> </Constraint> <NumValues> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>184.4</nPropValue> <nPropDigits>4</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>JCE</sCompiler> <sContributor>JCE</sContributor> <dateDateAdded>7/27/2003</dateDateAdded> <Property> <nPropNumber>1</nPropNumber> <Property-MethodID> <PropertyGroup> <CompositionAtPhaseEquilibrium> <ePropName>Eutectic composition: mole fraction</ePropName> <eMethodName>Derived from phase diagram analysis</eMethodName> </CompositionAtPhaseEquilibrium> </PropertyGroup> <RegNum> <nOrgNum>7</nOrgNum> </RegNum> </Property-MethodID> <PropPhaseID> <ePropPhase>Crystal</ePropPhase> </PropPhaseID> <ePresentation>Direct value, X</ePresentation> </Property> <PhaseID> <ePhase>Crystal</ePhase> <RegNum> <nOrgNum>7</nOrgNum> </RegNum> </PhaseID> <PhaseID> <ePhase>Crystal</ePhase> <RegNum> <nOrgNum>1</nOrgNum> </RegNum> </PhaseID> <PhaseID> <ePhase>Liquid</ePhase> </PhaseID> <PhaseID> <ePhase>Air at 1 atmosphere</ePhase> </PhaseID> <Constraint> <ConstraintID> <ConstraintType> <ePressure>Pressure, kPa</ePressure> </ConstraintType> </ConstraintID> <ConstraintPhaseID> <eConstraintPhase>Crystal</eConstraintPhase> </ConstraintPhaseID> <nConstraintValue>101.325</nConstraintValue> <nConstrDigits>6</nConstrDigits> </Constraint> <NumValues> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>.987</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>JCE</sCompiler> <sContributor>JCE</sContributor> <dateDateAdded>7/27/2003</dateDateAdded> <Property> <nPropNumber>1</nPropNumber> <Property-MethodID> <PropertyGroup> <PhaseTransition> <ePropName>Solid-liquid equilibrium temperature, K</ePropName> <eMethodName>Visual observation</eMethodName> </PhaseTransition> </PropertyGroup> </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>101.3</nConstraintValue> <nConstrDigits>4</nConstrDigits> </Constraint> <Variable> <nVarNumber>1</nVarNumber> <VariableID> <VariableType> <eComponentComposition>Mole fraction</eComponentComposition> </VariableType> <RegNum> <nOrgNum>7</nOrgNum> </RegNum> </VariableID> <VarPhaseID> <eVarPhase>Liquid</eVarPhase> </VarPhaseID> </Variable> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>0</nVarValue> <nVarDigits>0</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>274.42</nPropValue> <nPropDigits>5</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.0592</nVarValue> <nVarDigits>3</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>271.67</nPropValue> <nPropDigits>5</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.1028</nVarValue> <nVarDigits>4</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>270.15</nPropValue> <nPropDigits>5</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.1531</nVarValue> <nVarDigits>4</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>268.62</nPropValue> <nPropDigits>5</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.2011</nVarValue> <nVarDigits>4</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>267.06</nPropValue> <nPropDigits>5</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.2508</nVarValue> <nVarDigits>4</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>265.44</nPropValue> <nPropDigits>5</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.3035</nVarValue> <nVarDigits>4</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>263.63</nPropValue> <nPropDigits>5</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.3517</nVarValue> <nVarDigits>4</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>261.71</nPropValue> <nPropDigits>5</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.4017</nVarValue> <nVarDigits>4</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>259.64</nPropValue> <nPropDigits>5</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.4508</nVarValue> <nVarDigits>4</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>257.64</nPropValue> <nPropDigits>5</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.5011</nVarValue> <nVarDigits>4</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>255.47</nPropValue> <nPropDigits>5</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.5513</nVarValue> <nVarDigits>4</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>253.27</nPropValue> <nPropDigits>5</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.6002</nVarValue> <nVarDigits>4</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>251</nPropValue> <nPropDigits>5</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.6506</nVarValue> <nVarDigits>4</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>248.26</nPropValue> <nPropDigits>5</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.7006</nVarValue> <nVarDigits>4</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>245.01</nPropValue> <nPropDigits>5</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.7505</nVarValue> <nVarDigits>4</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>240.61</nPropValue> <nPropDigits>5</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.7982</nVarValue> <nVarDigits>4</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>234.71</nPropValue> <nPropDigits>5</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.8504</nVarValue> <nVarDigits>4</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>225.61</nPropValue> <nPropDigits>5</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.8998</nVarValue> <nVarDigits>4</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>213.19</nPropValue> <nPropDigits>5</nPropDigits> </PropertyValue> </NumValues> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>.9483</nVarValue> <nVarDigits>4</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>196.2</nPropValue> <nPropDigits>5</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>JCE</sCompiler> <sContributor>JCE</sContributor> <dateDateAdded>8/4/2003</dateDateAdded> <Property> <nPropNumber>1</nPropNumber> <Property-MethodID> <PropertyGroup> <PhaseTransition> <ePropName>Solid-liquid equilibrium temperature, K</ePropName> <eMethodName>Visual observation</eMethodName> </PhaseTransition> </PropertyGroup> </Property-MethodID> <PropPhaseID> <ePropPhase>Liquid</ePropPhase> </PropPhaseID> <ePresentation>Direct value, X</ePresentation> </Property> <PhaseID> <ePhase>Liquid</ePhase> </PhaseID> <PhaseID> <ePhase>Crystal</ePhase> <RegNum> <nOrgNum>7</nOrgNum> </RegNum> </PhaseID> <Constraint> <ConstraintID> <ConstraintType> <ePressure>Pressure, kPa</ePressure> </ConstraintType> </ConstraintID> <nConstraintValue>101.3</nConstraintValue> <nConstrDigits>4</nConstrDigits> </Constraint> <Variable> <nVarNumber>1</nVarNumber> <VariableID> <VariableType> <eComponentComposition>Mole fraction</eComponentComposition> </VariableType> <RegNum> <nOrgNum>7</nOrgNum> </RegNum> </VariableID> <VarPhaseID> <eVarPhase>Liquid</eVarPhase> </VarPhaseID> </Variable> <NumValues> <VariableValue> <nVarNumber>1</nVarNumber> <nVarValue>1</nVarValue> <nVarDigits>5</nVarDigits> </VariableValue> <PropertyValue> <nPropNumber>1</nPropNumber> <nPropValue>184.43</nPropValue> <nPropDigits>5</nPropDigits> </PropertyValue> </NumValues> </PureOrMixtureData> </DataReport>