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Numerical modeling of high-pressure phase-equilibria data using neural networks

Thesis (MEng)--Stellenbosch University, 2020.

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Main Author: Coetzee, Annelette
Other Authors: Schwarz, Cara Elsbeth
Format: Thesis
Language:en_ZA
Published: Stellenbosch : Stellenbosch University 2020
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access_status_str Open Access
author Coetzee, Annelette
author2 Schwarz, Cara Elsbeth
author_browse Coetzee, Annelette
Schwarz, Cara Elsbeth
author_facet Schwarz, Cara Elsbeth
Coetzee, Annelette
author_sort Coetzee, Annelette
collection Thesis
dc_rights_str_mv Stellenbosch University
description Thesis (MEng)--Stellenbosch University, 2020.
format Thesis
id oai:scholar.sun.ac.za:10019.1/109277
institution Stellenbosch University (South Africa)
language en_ZA
last_indexed 2026-06-10T12:43:15.981Z
license_str Other — see source repository
provenance_str_mv Harvested via OAI-PMH from SUNScholar — Stellenbosch University Repository
publishDate 2020
publishDateRange 2020
publishDateSort 2020
publisher Stellenbosch : Stellenbosch University
publisherStr Stellenbosch : Stellenbosch University
record_format dspace
source_str SUNScholar — Stellenbosch University Repository
spelling oai:scholar.sun.ac.za:10019.1/109277 Numerical modeling of high-pressure phase-equilibria data using neural networks Coetzee, Annelette Schwarz, Cara Elsbeth Knoetze, Johannes Hendrik Stellenbosch University. Faculty of Engineering. Dept. of Process Engineering. High pressure UCTD Equilibrium, Liquid-liquid Vapors Binary vapor systems Artificial Neural Networks Thesis (MEng)--Stellenbosch University, 2020. ENGLISH ABSTRACT: The design of process systems is greatly dependent on phase behaviour data, which can be predicted using equations of state(EOSs). These models, however, often fail to predict the behaviour near the mixture critical region. A more accurate and reliable method for predicting thermodynamic behaviour in the vicinity of the mixture critical region is therefore required. The aim of this project was to model the vapour-liquid equilibrium of binary systems containing supercritical CO2 and hydrocarbons using Artificial Neural Networks (ANNs). The bubble and dew point pressures were predicted as a function of functional group, a centric factor, critical temperature and pressure of the hydrocarbon, system temperature and CO2composition of the liquid and vapour phases.The ability of ANNs to predict the vapour-liquid phase equilibrium of binary systems was evaluated by modelling different systems and comparing the results to experimental data and EOS models. Case study 1 considered binary systems containing only CO2and alkanes. Case study 2 considered binary systems of CO2and various hydrocarbons, increasing the complexity by adding various functional groups. The hydrocarbons included alkanes, alcohols and carboxylic acids. The modelled results from case study 1 and 2 showed that the phase equilibrium of both simple and complex binary systems can be modelled using ANNs. After investigating the structure of the neural networks, the chain length and critical pressure of the hydrocarbon were eliminated as input parameters for case studies 1 and 2. The system temperature and liquid and vapour compositions of CO2were relatively more important compared to other input parameters for case study 1 where the critical and system temperatures and CO2composition of the vapour phase had a higher relative importance for case study 2. Using a feed forward neural network with two hidden layers and the log-sigmoid transfer function resulted in the optimum results for both these studies. Case study 1 and 2 resulted in acceptable 𝑅2and 𝐴𝐴𝐷%values for the training and testing data over the entire range. 𝑅2was 0.992 and 0.991 for case study 1 and 0.949 and 0.995 for case study 2 for the training and testing data sets. 𝐴𝐴𝐷%was 9.7% and 5.6% for case study 1 and 16.4% and 7.1% for case study 2 for the training and testing data sets. The ANN models were able to predict the phase behaviour over the entire range of compositions including the mixture critical region, whereas the EOS correlation models (the RK-Aspen EOS)failed to converge in the mixture critical region. Case study 3 considered the optimisation of ANNs as used in published articles by using the methodology and outcomes as used and concluded in case studies 1 and 2. The main difference in the methodology was the way the validation and test sets were divided: these sets consisted of complete binary systems instead of single data points extracted from binary systems. Although worse results were obtained using this methodology, the results were still acceptable. Using two hidden layers improved the accuracy of the results obtained by case study 3. AFRIKAANSE OPSOMMING: Raadpleeg teks vir opsomming Masters 2020-11-27T08:01:50Z 2021-01-31T19:42:29Z 2020-11-27T08:01:50Z 2021-01-31T19:42:29Z 2020-12 Thesis http://hdl.handle.net/10019.1/109277 en_ZA Stellenbosch University 231 pages application/pdf Stellenbosch : Stellenbosch University
spellingShingle High pressure
UCTD
Equilibrium, Liquid-liquid
Vapors
Binary vapor systems
Artificial Neural Networks
Coetzee, Annelette
Numerical modeling of high-pressure phase-equilibria data using neural networks
title Numerical modeling of high-pressure phase-equilibria data using neural networks
title_full Numerical modeling of high-pressure phase-equilibria data using neural networks
title_fullStr Numerical modeling of high-pressure phase-equilibria data using neural networks
title_full_unstemmed Numerical modeling of high-pressure phase-equilibria data using neural networks
title_short Numerical modeling of high-pressure phase-equilibria data using neural networks
title_sort numerical modeling of high pressure phase equilibria data using neural networks
topic High pressure
UCTD
Equilibrium, Liquid-liquid
Vapors
Binary vapor systems
Artificial Neural Networks
url http://hdl.handle.net/10019.1/109277
work_keys_str_mv AT coetzeeannelette numericalmodelingofhighpressurephaseequilibriadatausingneuralnetworks