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...
Guardado en:
Autor principal: | |
---|---|
Formato: | article |
Lenguaje: | EN RU UK |
Publicado: |
PC Technology Center
2021
|
Materias: | |
Acceso en línea: | https://doaj.org/article/17a36a4776854b0c82375b20ba2fea5b |
Etiquetas: |
Agregar Etiqueta
Sin Etiquetas, Sea el primero en etiquetar este registro!
|
id |
oai:doaj.org-article:17a36a4776854b0c82375b20ba2fea5b |
---|---|
record_format |
dspace |
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 |
_version_ |
1718444821791637504 |