Evidence map›Paper›PMID 36812039›Full record

ArticleJournal of chemical and engineering data2023

Isobaric Vapor-Liquid Equilibrium Data for Tetrahydrofuran + Acetic Acid and Tetrahydrofuran + Trichloroethylene Mixtures.

Vyomesh M Parsana, Sachin Parikh, Keval Ziniya, Hirvita Dave, Piyush Gadhiya, Kedar Joshi, Dolly Gandhi, Thijs J H Vlugt, Mahinder Ramdin

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Article in Journal of chemical and engineering data, 2023. The graph could read no effect estimate from its abstract, so it casts no vote on the map. Not yet cited in PubMed.

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1 · What the graph read from it

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The abstract states no effect estimate the extractor could read, or names no intervention and outcome on the map, so this paper lights no cell and moves no belief. It is still indexed, cited and linked below.

2 · The registry

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3 · Its place in the literature

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4 · The record

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5 · Who and what money

Authors and funding

9 authors.

Vyomesh M ParsanaChemical Engineering Department, V.V.P. Engineering College, Gujarat Technological University, Rajkot-360005, Gujarat, India.ORCID https://orcid.org/0000-0002-7473-1354
Sachin ParikhDepartment of Chemical Engineering, L.D. College of Engineering, Gujarat Technological University, Ahmedabad-380015, Gujarat, India.
Keval ZiniyaChemical Engineering Department, V.V.P. Engineering College, Gujarat Technological University, Rajkot-360005, Gujarat, India.
Hirvita DaveChemical Engineering Department, V.V.P. Engineering College, Gujarat Technological University, Rajkot-360005, Gujarat, India.
Piyush GadhiyaDepartment of Chemical Engineering, Government Polytechnic Rajkot, Rajkot-360003, Gujarat, India.
Kedar JoshiChemical Engineering Department, Vishwakarma Government Engineering College, Gujarat Technological University, Ahmedabad-382424, Gujarat, India.ORCID https://orcid.org/0000-0002-4993-2189
Dolly GandhiChemical Engineering Department, Vishwakarma Government Engineering College, Gujarat Technological University, Ahmedabad-382424, Gujarat, India.
Thijs J H VlugtEngineering Thermodynamics, Process & Energy Department, Faculty of Mechanical, Maritime and Materials Engineering, Delft University of Technology, Leeghwaterstraat 39, 2628 CBDelft, The Netherlands.ORCID https://orcid.org/0000-0003-3059-8712
Mahinder RamdinEngineering Thermodynamics, Process & Energy Department, Faculty of Mechanical, Maritime and Materials Engineering, Delft University of Technology, Leeghwaterstraat 39, 2628 CBDelft, The Netherlands.ORCID https://orcid.org/0000-0002-8476-7035

Funding

No grant is acknowledged in the PubMed record.

6 · The paper itself

Abstract

Vapor-liquid equilibrium (VLE) data for the binary systems tetrahydrofuran (THF) + acetic acid (AA) and THF + trichloroethylene (TCE) were measured under isobaric conditions using an ebulliometer. The boiling temperatures for the systems (THF + AA/THF + TCE) are reported for 13/15 compositions and five/six different pressures ranging from 50.2/60.0 to 101.1/101.3 kPa, respectively. The THF + AA system shows simple phase behavior with no azeotrope formation. The THF + TCE system does not exhibit azeotrope formation but seems to have a pinch point close to the pure end of TCE. The nonrandom two-liquid (NRTL) and universal quasichemical (UNIQUAC) activity coefficient models were used to accurately fit the binary (

Identifiers

PMID36812039
PMCPMC9923677

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