z-logo
open-access-imgOpen Access
Isobaric vapour-liquid equilibrium calculations of binary systems using neural network
Author(s) -
Mehmet Bilgin
Publication year - 2004
Publication title -
journal of the serbian chemical society
Language(s) - English
Resource type - Journals
eISSN - 1820-7421
pISSN - 0352-5139
DOI - 10.2298/jsc0409669b
Subject(s) - unifac , azeotrope , methylcyclohexane , isobaric process , thermodynamics , activity coefficient , binary number , vapor–liquid equilibrium , chemistry , artificial neural network , group contribution method , toluene , phase equilibrium , organic chemistry , computer science , mathematics , physics , distillation , arithmetic , aqueous solution , phase (matter) , machine learning
A model on a feed forward back propagation neural network was em- ployed to calculate the isobaric vapour-liquid equilibrium (VLE) data at 40, 66.67, and 101.32 0.02 kPa for the methylcyclohexane - toluene and isopropanol - methyl isobutyl ketone binary systems, which are composed of different chemical structures (cyclic, aromatic, alcohol and ketone) and do not show azeotrope behav- iour. Half of the experimental VLE data only were assigned into the designed frame- work as training patterns in order to estimate the VLE data over the whole composi- tion range at the mentioned pressures. The results were compared with the data cal- culated by the two classical models used in this field, the UNIFAC and Margules models. In all cases the deviations the experimental activity coefficients and those calculated by the neural network model (NNET) were lower than those obtained us- ing the Margules and UNIFAC models.

The content you want is available to Zendy users.

Already have an account? Click here to sign in.
Having issues? You can contact us here
Accelerating Research

Address

John Eccles House
Robert Robinson Avenue,
Oxford Science Park, Oxford
OX4 4GP, United Kingdom