Vapor liquid equilibrium measurements for clean fuel processes

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dc.contributor Aalto-yliopisto fi
dc.contributor Aalto University en
dc.contributor.author Kim, Younghun
dc.date.accessioned 2012-02-17T06:49:23Z
dc.date.available 2012-02-17T06:49:23Z
dc.date.issued 2005-03-04
dc.identifier.isbn 951-22-7626-7
dc.identifier.issn 1236-875X
dc.identifier.uri https://aaltodoc.aalto.fi/handle/123456789/2537
dc.description.abstract This thesis is based on seven publications dealing with the Vapor Liquid Equilibrium (VLE) measurements which are necessary for pure components process. Two VLE measurements sections were comprised in this thesis. Firstly, VLE runs were conducted with a circulation still at both atmospheric pressure and isothermal conditions under low atmospheric pressure. Secondly, the static apparatus has been used in isothermal VLE for six binary pairs of C4 hydrocarbons and 2-propanone in a range from 69.6 kPa to 610.9 kPa. In addition, the VLE modeling was considered to determine the parameters in thermodynamic models. The selected components are in area of great industrial interest in view of developing gasoline additives to replace MTBE (2-methoxy-2-methylpropane), such as transform old MTBE plants to produce isooctene. Especially ETBE (2-Ethoxy-2-methylpropane) has emerged as an alternative to MTBE, because ETBE can be produced from ethanol made of renewable resources. The experimental data were correlated using activity coefficient models for the liquid phase and equation of state (EOS) for the vapor phase. These models were also compared with a predictive activity coefficient models. The estimations made with various different predictive coefficient models gave worse description of the measurements than by fitting the data with the Wilson equation. The experimental apparatus and the procedure presented were shown to be reliable, particularly the computer-controlled static apparatus. Moreover, these results seem to be reliable since they passed thermodynamic consistency tests. Most VLE and excess enthalpy measurements in this thesis are for binary systems that have not been measured previously. en
dc.format.extent 44, [app]
dc.format.mimetype application/pdf
dc.language.iso en en
dc.publisher Helsinki University of Technology en
dc.publisher Teknillinen korkeakoulu fi
dc.relation.ispartofseries Chemical engineering report series en
dc.relation.ispartofseries Kemian laitetekniikan raporttisarja fi
dc.relation.ispartofseries 48 en
dc.relation.haspart Uusi-Kyyny, P., Tarkiainen, V., Kim, Y., Ketola, R. A. and Aittamaa, J., 2003. Vapor liquid equilibria for ethanol + 2,4,4-trimethyl-1-pentene and 2-propanol + 2,4,4-trimethyl-1-pentene at 101 kPa. Journal of Chemical and Engineering Data 48, pages 280-285.
dc.relation.haspart Pokki, J.-P., Řehák, K., Kim, Y., Matouš, J. and Aittamaa, J., 2003. Vapor-liquid equilibrium data at 343 K and excess molar enthalpy data at 298 K for the binary systems of ethanol + 2,4,4-trimethyl-1-pentene and 2-propanol + 2,4,4-trimethyl-1-pentene. Journal of Chemical and Engineering Data 48, pages 75-80.
dc.relation.haspart Kim, Y., Pokki, J.-P., Řehák, K., Matouš, J. and Aittamaa, J., 2004. Excess enthalpy and vapor-liquid equilibrium at atmospheric pressure for the binary systems 2-methyl-2-propanol + 2,4,4-trimethyl-1-pentene and 2-butanol + 2,4,4-trimethyl-1-pentene. Journal of Chemical and Engineering Data 49, pages 246-250.
dc.relation.haspart Kim, Y., Keskinen, K. I. and Aittamaa, J., 2004. Vapor-liquid equilibrium for binary systems 2-propanol + 2-ethoxy-2-methylpropane and ethyl ethanoate + 2-ethoxy-2-methylpropane at 333 K and 2-propanone + 2-ethoxy-2-methylpropane at 323 K. Journal of Chemical and Engineering Data 49, pages 1273-1278.
dc.relation.haspart Kim, Y., Uusi-Kyyny, P., Pokki, J.-P., Pakkanen, M., Multala, R., Westerlund, L. M. and Aittamaa, J., 2004. Isothermal vapour-liquid equilibrium measurements for six binary systems of C4 hydrocarbons + 2-propanone. Fluid Phase Equilibria 226, pages 173-181.
dc.relation.haspart Uusi-Kyyny, P., Pokki, J.-P., Kim, Y. and Aittamaa, J., 2004. Isobaric vapor liquid equilibrium for 2,3-dimethyl-2-butene + methanol, + ethanol, + 2-propanol, or + 2-butanol at atmospheric pressure. Journal of Chemical and Engineering Data 49, pages 251-255.
dc.relation.haspart Kim, Y., Sapei, E., Keskinen, K. I. and Aittamaa, J., 2005. Vapor-liquid equilibrium for binary systems of 2-propanol + 1,1-diethoxyethane at 353 K, ethyl ethanoate + 1,1-diethoxyethane at 348 K, and 2-propanone + 1,1-diethoxyethane at 328 K. Journal of Chemical and Engineering Data, accepted for publication on 13.12.2004.
dc.subject.other Chemistry en
dc.subject.other Energy en
dc.title Vapor liquid equilibrium measurements for clean fuel processes en
dc.type G5 Artikkeliväitöskirja fi
dc.description.version reviewed en
dc.contributor.department Department of Chemical Technology en
dc.contributor.department Kemian tekniikan osasto fi
dc.subject.keyword VLE en
dc.subject.keyword MTBE en
dc.subject.keyword ETBE en
dc.identifier.urn urn:nbn:fi:tkk-004915
dc.type.dcmitype text en
dc.type.ontasot Väitöskirja (artikkeli) fi
dc.type.ontasot Doctoral dissertation (article-based) en
dc.contributor.lab Laboratory of Chemical Engineering and Plant Design en
dc.contributor.lab Kemian laitetekniikan ja tehdassuunnittelun laboratorio fi


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