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Geometric acceleration of complex chemical equilibrium calculations for inclusion in multiphysics and process models

Thesis (PhD (Metallurgical Engineering))--University of Pretoria, 2023.

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Other Authors: Zietsman, Johan
Format: Thesis
Language:English
Published: University of Pretoria 2023
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access_status_str Open Access
author2 Zietsman, Johan
author_browse Zietsman, Johan
author_facet Zietsman, Johan
collection Thesis
dc_rights_str_mv © 2023 University of Pretoria. All rights reserved. The copyright in this work vests in the University of Pretoria. No part of this work may be reproduced or transmitted in any form or by any means, without the prior written permission of the University of Pretoria.
description Thesis (PhD (Metallurgical Engineering))--University of Pretoria, 2023.
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institution University of Pretoria (South Africa)
language English
last_indexed 2026-06-10T12:38:08.659Z
license_str Other — see source repository
provenance_str_mv Harvested via OAI-PMH from UPSpace — University of Pretoria Institutional Repository
publishDate 2023
publishDateRange 2023
publishDateSort 2023
publisher University of Pretoria
publisherStr University of Pretoria
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spelling oai:repository.up.ac.za:2263/91657 Geometric acceleration of complex chemical equilibrium calculations for inclusion in multiphysics and process models Zietsman, Johan willem.ab.roos@gmail.com Roos, Willem Abraham Equilibrium calculations CALPHAD Acceleration Generic lever rule Gibbs phase rule Process and multiphysics models UCTD Thesis (PhD (Metallurgical Engineering))--University of Pretoria, 2023. Incorporating multi-component, multi-phase, high-temperature, complex chemical equilibrium calculations into multiphysics and process models can provide valuable insights into industrial processes and equipment that current modelling methods and measurements cannot. The equilibrium state of a thermochemical system is determined by minimising the Gibbs energy for a given set of system component concentrations, temperature, and pressure, and becomes computationally expensive when a large number of these calculations have to be performed. This makes direct integration of chemical equilibrium calculations into models infeasible. There have been many attempts to, in one way or another, accelerate these calculations. The strengths of these existing acceleration methods, together with fundamental thermochemical theory, were used to conceptualise and develop a new accelerator algorithm. The accelerator algorithm uses a system's phase diagram and the Gibbs phase rule to map the thermochemical system to geometric space by storing calculated physical and thermochemical properties in-situ for later recall and interpolation. Linear interpolation with the lever rule in geometric space is less computationally expensive than Gibbs energy minimisation. The advantage of populating a database in-situ is that data is only generated and stored in the regions accessed by the model as it is being solved. The accelerator algorithm is based on established thermochemical theory, and the generality thereof allows the accelerator to be used in any system, regardless of the number of components. The performance of the accelerator algorithm was tested on a number of two- and three-component systems as well as on two industry-related processes; a simplified four-component ilmenite smelting system and a simplified five-component iron- and steelmaking system. As the number of system components increase, so does the computational expense of equilibrium calculations. This translated to larger acceleration factors being achieved as the number of system components increased -- from as high as 20 in two-component systems to 1000 in the four- and five-component systems. Interpolation errors made on phase compositions were in the order of 10E-2 mole\mole and less. This would translate to an interpolated phase composition being accurate to within 99% of the calculated phase composition. The majority of interpolation errors made on physical and thermochemical properties were in the order of 1% and less. The developed algorithm showed noteworthy acceleration of equilibrium calculations when tested on the two industry-related processes while maintaining acceptable levels of accuracy. There is great potential for the accelerator algorithm to make the inclusion of equilibrium calculations in models with many system components feasible. The performance of the accelerator can be improved by transferring the algorithm to a more computationally efficient compiled programming language and utilising a more performant database system. Materials Science and Metallurgical Engineering PhD (Metallurgical Engineering) Unrestricted 2023-07-27T12:54:28Z 2023-07-27T12:54:28Z 2023-09-05 2023-07-27 Thesis * S2023 http://hdl.handle.net/2263/91657 en © 2023 University of Pretoria. All rights reserved. The copyright in this work vests in the University of Pretoria. No part of this work may be reproduced or transmitted in any form or by any means, without the prior written permission of the University of Pretoria. application/pdf University of Pretoria
spellingShingle Equilibrium calculations
CALPHAD
Acceleration
Generic lever rule
Gibbs phase rule
Process and multiphysics models
UCTD
Geometric acceleration of complex chemical equilibrium calculations for inclusion in multiphysics and process models
title Geometric acceleration of complex chemical equilibrium calculations for inclusion in multiphysics and process models
title_full Geometric acceleration of complex chemical equilibrium calculations for inclusion in multiphysics and process models
title_fullStr Geometric acceleration of complex chemical equilibrium calculations for inclusion in multiphysics and process models
title_full_unstemmed Geometric acceleration of complex chemical equilibrium calculations for inclusion in multiphysics and process models
title_short Geometric acceleration of complex chemical equilibrium calculations for inclusion in multiphysics and process models
title_sort geometric acceleration of complex chemical equilibrium calculations for inclusion in multiphysics and process models
topic Equilibrium calculations
CALPHAD
Acceleration
Generic lever rule
Gibbs phase rule
Process and multiphysics models
UCTD
url http://hdl.handle.net/2263/91657