Isobaric and Isothermal Vapor-Liquid Equilibria for the Binary System of Water plus Formic Acid at 99.41 kPa, 388.15 K, and 398.15 K
The result's identifiers
Result code in IS VaVaI
<a href="https://www.isvavai.cz/riv?ss=detail&h=RIV%2F60461373%3A22310%2F16%3A43902210" target="_blank" >RIV/60461373:22310/16:43902210 - isvavai.cz</a>
Result on the web
<a href="http://pubs.acs.org/doi/abs/10.1021/acs.jced.6b00139" target="_blank" >http://pubs.acs.org/doi/abs/10.1021/acs.jced.6b00139</a>
DOI - Digital Object Identifier
<a href="http://dx.doi.org/10.1021/acs.jced.6b00139" target="_blank" >10.1021/acs.jced.6b00139</a>
Alternative languages
Result language
angličtina
Original language name
Isobaric and Isothermal Vapor-Liquid Equilibria for the Binary System of Water plus Formic Acid at 99.41 kPa, 388.15 K, and 398.15 K
Original language description
In the process of methyl formate hydrolysis, it is necessary to separate water from formic acid. Rectification is one of the suitable methods to achieve this. However, vapor liquid equilibrium data are essential for the rectification unit design, and these are either not available in the literature at all, or when available are significantly scattered. The water + formic acid binary system forms a maximum-boiling azeotrope, and its behavior is nonideal both in liquid and vapor phases. In this paper, we are presenting the vapor liquid equilibrium data for the above-specified binary system. The isobaric and isothermal data have been measured under atmospheric pressure and at the temperatures of 388.15 and 398.15 K. We have found, based on the value of the average absolute deviation, that the UNIQUAC-Hayden O'Connell combined model is the best fitting for the measured data plotting. On the basis of this combined model, we are able to estimate the azeotropic point composition at elevated pressure levels. In addition, our data can be reliably used in the future design of a rectification unit.
Czech name
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Czech description
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Classification
Type
J<sub>x</sub> - Unclassified - Peer-reviewed scientific article (Jimp, Jsc and Jost)
CEP classification
CI - Industrial chemistry and chemical engineering
OECD FORD branch
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Result continuities
Project
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Continuities
I - Institucionalni podpora na dlouhodoby koncepcni rozvoj vyzkumne organizace
Others
Publication year
2016
Confidentiality
S - Úplné a pravdivé údaje o projektu nepodléhají ochraně podle zvláštních právních předpisů
Data specific for result type
Name of the periodical
Journal of Chemical Engineering Data
ISSN
0021-9568
e-ISSN
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Volume of the periodical
61
Issue of the periodical within the volume
10
Country of publishing house
US - UNITED STATES
Number of pages
8
Pages from-to
3398-3405
UT code for WoS article
000385606900003
EID of the result in the Scopus database
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