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			<yrYrPub>2009</yrYrPub>
			<sAuthor1>seg</sAuthor1>
			<sAuthor2>mar</sAuthor2>
			<nAuthorn>0</nAuthorn>
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		<eType>journal</eType>
		<eSourceType>Original</eSourceType>
		<sAuthor>Segovia, J. J.[Jose J.]</sAuthor>
		<sAuthor>Martin, M. C.</sAuthor>
		<sAuthor>Vega-Maza, D.[David]</sAuthor>
		<sAuthor>Chamorro, C. R.[Cesar R.]</sAuthor>
		<sAuthor>Villamanan, M. A.[Miguel A.]</sAuthor>
		<sPubName>J. Chem. Thermodyn.</sPubName>
		<yrPubYr>2009</yrPubYr>
		<dateCit>2009-06-30</dateCit>
		<sTitle>Thermodynamics of biofuels: Excess enthalpies for binary mixtures involving  ethyl 1,1-dimethylethyl ether and hydrocarbons at different temperatures using a new flow calorimeter</sTitle>
		<sKeyword>Excess</sKeyword>
		<sKeyword>molar enthalpy</sKeyword>
		<sKeyword>ETBE</sKeyword>
		<sKeyword>Heptane</sKeyword>
		<sKeyword>Cyclohexane</sKeyword>
		<sKeyword>Toluene</sKeyword>
		<sDOI>10.1016/j.jct.2008.12.004</sDOI>
		<sVol>41</sVol>
		<sPage>759-763</sPage>
	</Citation>
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		<sStandardInChI>InChI=1S/C6H12/c1-2-4-6-5-3-1/h1-6H2</sStandardInChI>
		<sCommonName>cyclohexane</sCommonName>
		<sFormulaMolec>C6H12</sFormulaMolec>
		<Sample>
			<nSampleNm>1</nSampleNm>
			<eSource>Commercial source</eSource>
			<purity>
				<nStep>1</nStep>
				<nUnknownPerCent>99.5</nUnknownPerCent>
				<nUnknownPerCentDigits>3</nUnknownPerCentDigits>
				<eAnalMeth>Gas chromatography</eAnalMeth>
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		<sStandardInChI>InChI=1S/C6H14/c1-3-5-6-4-2/h3-6H2,1-2H3</sStandardInChI>
		<sCommonName>hexane</sCommonName>
		<sFormulaMolec>C6H14</sFormulaMolec>
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		<eExpPurpose>Principal objective of the work</eExpPurpose>
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		<dateDateAdded>5/26/2009</dateDateAdded>
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				<sUncertEvaluator>Author</sUncertEvaluator>
				<nUncertLevOfConfid>95</nUncertLevOfConfid>
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				<ePhase>Liquid</ePhase>
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			<ConstraintID>
				<ConstraintType>
					<eTemperature>Temperature, K</eTemperature>
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			<nConstraintValue>298.15</nConstraintValue>
			<nConstrDigits>5</nConstrDigits>
			<ConstrUncertainty>
				<sUncertEvaluator>Author</sUncertEvaluator>
				<nStdUncertValue>.001</nStdUncertValue>
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		<Constraint>
			<ConstraintID>
				<ConstraintType>
					<ePressure>Pressure, kPa</ePressure>
				</ConstraintType>
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			<nConstraintValue>101</nConstraintValue>
			<nConstrDigits>3</nConstrDigits>
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					<eComponentComposition>Mole fraction</eComponentComposition>
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