Vapor–Liquid Equilibria of Nitrogen + Diethyl Ether and Nitrogen + 1,1,1,2,2,4,5,5,5-Nonafluoro-4-(trifluoromethyl)-3-pentanone by Experiment, Peng–Robinson and PC-SAFT Equations of State
dc.contributor.author | Linnemann, Matthias | |
dc.contributor.author | Vrabec, Jadran | |
dc.date.accessioned | 2020-04-27T07:50:27Z | |
dc.date.available | 2020-04-27T07:50:27Z | |
dc.date.issued | 2017-06-01 | |
dc.description.abstract | The saturated liquid line of the systems nitrogen (N2) + diethyl ether and N2 + 1,1,1,2,2,4,5,5,5-nonafluoro-4-(trifluoromethyl)-3-pentanone (Novec 649) is measured along three isotherms, that is, 390, 420, and 450 K and 360, 390, and 420 K, respectively. The employed gas solubility apparatus, based on the synthetic method, allows to measure points up to the critical region of these mixtures. The experimental data are used to correlate the Peng–Robinson and PC-SAFT equations of state (EOS). For the parametrization of the system, N2 + diethyl ether the Peng–Robinson EOS is combined with the Huron–Vidal mixing rule and the non-random two-liquid (NRTL) excess Gibbs energy model; for the system N2 + Novec 649 the quadratic mixing rule is used. | en |
dc.identifier.eissn | 1520-5134 | |
dc.identifier.issn | 0021-9568 | |
dc.identifier.uri | https://depositonce.tu-berlin.de/handle/11303/11014 | |
dc.identifier.uri | http://dx.doi.org/10.14279/depositonce-9906 | |
dc.language.iso | en | en |
dc.relation.ispartof | 10.14279/depositonce-9842 | |
dc.rights.uri | http://rightsstatements.org/vocab/InC/1.0/ | en |
dc.subject.ddc | 660 Chemische Verfahrenstechnik | de |
dc.subject.other | liquids | en |
dc.subject.other | theoretical chemistry | en |
dc.subject.other | computational chemistry | en |
dc.subject.other | ethers | en |
dc.subject.other | nitrogen ethyl groups | en |
dc.subject.other | solubility | en |
dc.title | Vapor–Liquid Equilibria of Nitrogen + Diethyl Ether and Nitrogen + 1,1,1,2,2,4,5,5,5-Nonafluoro-4-(trifluoromethyl)-3-pentanone by Experiment, Peng–Robinson and PC-SAFT Equations of State | en |
dc.type | Article | en |
dc.type.version | acceptedVersion | en |
dcterms.bibliographicCitation.doi | 10.1021/acs.jced.7b00217 | en |
dcterms.bibliographicCitation.issue | 7 | en |
dcterms.bibliographicCitation.journaltitle | Journal of Chemical and Engineering Data | en |
dcterms.bibliographicCitation.originalpublishername | American Chemical Society (ACS) | en |
dcterms.bibliographicCitation.originalpublisherplace | Columbus, Ohio | en |
dcterms.bibliographicCitation.pageend | 2114 | en |
dcterms.bibliographicCitation.pagestart | 2110 | en |
dcterms.bibliographicCitation.volume | 62 | en |
tub.accessrights.dnb | free | en |
tub.affiliation | Fak. 3 Prozesswissenschaften::Inst. Prozess- und Verfahrenstechnik::FG Thermodynamik und Thermische Verfahrenstechnik | de |
tub.affiliation.faculty | Fak. 3 Prozesswissenschaften | de |
tub.affiliation.group | FG Thermodynamik und Thermische Verfahrenstechnik | de |
tub.affiliation.institute | Inst. Prozess- und Verfahrenstechnik | de |
tub.publisher.universityorinstitution | Technische Universität Berlin | en |
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