Building a mathematical model of technological processes in the acetic acid synthesis reactor

The result of the study reported in this paper is the proposed mathematical model of technological processes occurring in the reactor for acetic acid synthesis. The initial parameters of the reactor considered were the value of the concentration of acetic acid at the reactor outlet, temperature, the...

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Autor principal: Zhanna Samojlova
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RU
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Publicado: PC Technology Center 2021
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Acceso en línea:https://doaj.org/article/17a36a4776854b0c82375b20ba2fea5b
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spelling oai:doaj.org-article:17a36a4776854b0c82375b20ba2fea5b2021-11-04T14:06:13ZBuilding a mathematical model of technological processes in the acetic acid synthesis reactor1729-37741729-406110.15587/1729-4061.2021.242816https://doaj.org/article/17a36a4776854b0c82375b20ba2fea5b2021-10-01T00:00:00Zhttp://journals.uran.ua/eejet/article/view/242816https://doaj.org/toc/1729-3774https://doaj.org/toc/1729-4061The result of the study reported in this paper is the proposed mathematical model of technological processes occurring in the reactor for acetic acid synthesis. The initial parameters of the reactor considered were the value of the concentration of acetic acid at the reactor outlet, temperature, the level of reaction mass, and pressure in the reactor. The input parameters included the amount of methanol and carbon monoxide supplied. Material and thermal balances of reactor technological processes were used to construct the mathematical model of the reactor. Fisher criterion was applied to test the mathematical model for adequacy. At the specified 5 % level of significance, the value of Fisher criterion for the concentration of acetic acid, temperature, and the level of reaction mass in the reactor does not exceed its critical value for a stationary mode. The reproducibility of the modeling results was tested using the Cochran criterion. The value of the Cochrane criterion, at the predefined 5 % level of significance, for the concentration of acetic acid, temperature, and the level of reaction mass in the reactor does not exceed its critical value for different modes. The relative error for the modeled output parameters was calculated. The relative error of the initial parameters did not exceed the level of 10 %. The model built makes it possible to calculate with satisfactory accuracy the value of the concentration of acetic acid at the reactor output, the temperature and level of the reaction mass in the reactor under a stationary mode. The resulting model could be used to automate the control of technological processes in the acetic acid synthesis reactor under a stationary mode. The study results open additional opportunities to manage the stationary mode of the reactorZhanna SamojlovaPC Technology Centerarticlestatic mathematical model of acetic acid synthesis reactorautomatic controltechnological processesTechnology (General)T1-995IndustryHD2321-4730.9ENRUUKEastern-European Journal of Enterprise Technologies, Vol 5, Iss 2 (113), Pp 94-104 (2021)
institution DOAJ
collection DOAJ
language EN
RU
UK
topic static mathematical model of acetic acid synthesis reactor
automatic control
technological processes
Technology (General)
T1-995
Industry
HD2321-4730.9
spellingShingle static mathematical model of acetic acid synthesis reactor
automatic control
technological processes
Technology (General)
T1-995
Industry
HD2321-4730.9
Zhanna Samojlova
Building a mathematical model of technological processes in the acetic acid synthesis reactor
description The result of the study reported in this paper is the proposed mathematical model of technological processes occurring in the reactor for acetic acid synthesis. The initial parameters of the reactor considered were the value of the concentration of acetic acid at the reactor outlet, temperature, the level of reaction mass, and pressure in the reactor. The input parameters included the amount of methanol and carbon monoxide supplied. Material and thermal balances of reactor technological processes were used to construct the mathematical model of the reactor. Fisher criterion was applied to test the mathematical model for adequacy. At the specified 5 % level of significance, the value of Fisher criterion for the concentration of acetic acid, temperature, and the level of reaction mass in the reactor does not exceed its critical value for a stationary mode. The reproducibility of the modeling results was tested using the Cochran criterion. The value of the Cochrane criterion, at the predefined 5 % level of significance, for the concentration of acetic acid, temperature, and the level of reaction mass in the reactor does not exceed its critical value for different modes. The relative error for the modeled output parameters was calculated. The relative error of the initial parameters did not exceed the level of 10 %. The model built makes it possible to calculate with satisfactory accuracy the value of the concentration of acetic acid at the reactor output, the temperature and level of the reaction mass in the reactor under a stationary mode. The resulting model could be used to automate the control of technological processes in the acetic acid synthesis reactor under a stationary mode. The study results open additional opportunities to manage the stationary mode of the reactor
format article
author Zhanna Samojlova
author_facet Zhanna Samojlova
author_sort Zhanna Samojlova
title Building a mathematical model of technological processes in the acetic acid synthesis reactor
title_short Building a mathematical model of technological processes in the acetic acid synthesis reactor
title_full Building a mathematical model of technological processes in the acetic acid synthesis reactor
title_fullStr Building a mathematical model of technological processes in the acetic acid synthesis reactor
title_full_unstemmed Building a mathematical model of technological processes in the acetic acid synthesis reactor
title_sort building a mathematical model of technological processes in the acetic acid synthesis reactor
publisher PC Technology Center
publishDate 2021
url https://doaj.org/article/17a36a4776854b0c82375b20ba2fea5b
work_keys_str_mv AT zhannasamojlova buildingamathematicalmodeloftechnologicalprocessesintheaceticacidsynthesisreactor
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