Please use this identifier to cite or link to this item:
https://hdl.handle.net/10321/4691
DC Field | Value | Language |
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dc.contributor.author | Tebbal, Zoubir | en_US |
dc.contributor.author | Ngema, Peterson Thokozani | en_US |
dc.contributor.author | Narasigadu, Caleb | en_US |
dc.contributor.author | Negadi, Latifa | en_US |
dc.contributor.author | Ramjugernath, Deresh | en_US |
dc.date.accessioned | 2023-03-28T13:22:53Z | - |
dc.date.available | 2023-03-28T13:22:53Z | - |
dc.date.issued | 2014-05 | - |
dc.identifier.citation | Tebbal, Z. et al. 2014. Vapor-liquid equilibrium data for binary systems of n-Dodecane + {Propan-1-ol, Butan-1-ol, 2-Methylpropan-1-ol} at 40 kPa. Journal of Chemical and Engineering Data. 59(5): 1710-1713. doi:10.1021/je500237g | en_US |
dc.identifier.issn | 0021-9568 | - |
dc.identifier.issn | 1520-5134 (Online) | - |
dc.identifier.other | isidoc: AH1KF | - |
dc.identifier.uri | https://hdl.handle.net/10321/4691 | - |
dc.description.abstract | Isobaric (T-x-y) binary vapor-liquid equilibrium (VLE) data were measured and modeled for the n-dodecane + {propan-1-ol, butan-1-ol, or 2-methylpropan-1-ol} systems at 40 kPa. A low pressure dynamic still, capable of measuring systems of high relative volatility, was used for the measurements. The vapor and liquid equilibrium compositions were determined using a gas chromatograph with a thermal conductivity detector. The experimental data were regressed using the combined method (γ-φ approach). The nonrandom two-liquid (NRTL) activity coefficient model was used to describe the liquid phase nonideality, and the vapor phase was assumed to be ideal. The NRTL model parameters were determined using nonlinear least-squares regression. The experimental data were found to be well correlated with the thermodynamic modeling. No azeotropic behavior has been observed. The three investigated systems show a large positive deviation from Raoult's law. © 2014 American Chemical Society. | en_US |
dc.format.extent | 4 p | en_US |
dc.language.iso | en | en_US |
dc.publisher | American Chemical Society (ACS) | en_US |
dc.relation.ispartof | Journal of Chemical and Engineering Data; Vol. 59, Issue 5 | en_US |
dc.subject | 0904 Chemical Engineering | en_US |
dc.subject | Chemical Engineering | en_US |
dc.title | Vapor-liquid equilibrium data for binary systems of n-Dodecane + {Propan-1-ol, Butan-1-ol, 2-Methylpropan-1-ol} at 40 kPa | en_US |
dc.type | Article | en_US |
dc.date.updated | 2023-03-27T14:49:44Z | - |
dc.identifier.doi | 10.1021/je500237g | - |
item.grantfulltext | open | - |
item.cerifentitytype | Publications | - |
item.openairetype | Article | - |
item.languageiso639-1 | en | - |
item.fulltext | With Fulltext | - |
item.openairecristype | http://purl.org/coar/resource_type/c_18cf | - |
Appears in Collections: | Research Publications (Engineering and Built Environment) |
Files in This Item:
File | Description | Size | Format | |
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Zoubir et al_2014.pdf | Article | 309.16 kB | Adobe PDF | View/Open |
JCED Copyright Clearance.docx | Copyright Clearance | 198.27 kB | Microsoft Word XML | View/Open |
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