Modeling and simulation of ethane cracker reactor using Aspen Plus
The main aim of the work was to investigate if simple reactor blocks could be combined to adequately represent complex reactor configurations; with the objectives of selecting an appropriate reaction scheme, creating a working simulation and validating the results obtained from the simulation. An et...
Main Authors: | , , , |
---|---|
Format: | Article |
Language: | English |
Published: |
Elsevier
2023-01-01
|
Series: | South African Journal of Chemical Engineering |
Subjects: | |
Online Access: | http://www.sciencedirect.com/science/article/pii/S1026918522001056 |
_version_ | 1797955444544634880 |
---|---|
author | Tristan Lee Zebert David Lokhat Swamy Kurella B.C. Meikap |
author_facet | Tristan Lee Zebert David Lokhat Swamy Kurella B.C. Meikap |
author_sort | Tristan Lee Zebert |
collection | DOAJ |
description | The main aim of the work was to investigate if simple reactor blocks could be combined to adequately represent complex reactor configurations; with the objectives of selecting an appropriate reaction scheme, creating a working simulation and validating the results obtained from the simulation. An ethane cracker reactor is simulated using Aspen Plus, for a molecular reaction scheme, made up of seven reactions and eight hydrocarbon components; using the kinetics and reactor geometrics. Several assumptions were made such that the fired furnace reactor could be modeled as a series of two plug flow reactors using Aspen Plus. Modeling of a fired furnace reactor for the cracking of ethane is made difficult by the inherent separation between the convection and radiation sections; a difficulty which was overcome by separating the convection region and the radiation region of the fired furnace reactor into two simulations such that temperatures were solved for iteratively. A firebox simulation was created with the intent of finding the optimal fuel and air flow rates that would supply the fired furnace rector with the required 2490 kW; these flow rates were found to be 190 kmol hr−1 and 60 kmol hr−1. |
first_indexed | 2024-04-10T23:34:20Z |
format | Article |
id | doaj.art-c5103ac1fc9245588bb709fa4c66da8c |
institution | Directory Open Access Journal |
issn | 1026-9185 |
language | English |
last_indexed | 2024-04-10T23:34:20Z |
publishDate | 2023-01-01 |
publisher | Elsevier |
record_format | Article |
series | South African Journal of Chemical Engineering |
spelling | doaj.art-c5103ac1fc9245588bb709fa4c66da8c2023-01-12T04:18:28ZengElsevierSouth African Journal of Chemical Engineering1026-91852023-01-0143204214Modeling and simulation of ethane cracker reactor using Aspen PlusTristan Lee Zebert0David Lokhat1Swamy Kurella2B.C. Meikap3Discipline of Chemical Engineering, School of Engineering, Howard College, University of Kwazulu-Natal (UKZN), Durban 4041, South AfricaDiscipline of Chemical Engineering, School of Engineering, Howard College, University of Kwazulu-Natal (UKZN), Durban 4041, South AfricaDepartment of Chemical Engineering, National Institute of Technology Srinagar, Jammu and Kashmir, India; Corresponding author at: Department of Chemical Engineering, National Institute of Technology Srinagar, Jammu and Kashmir, India.Discipline of Chemical Engineering, School of Engineering, Howard College, University of Kwazulu-Natal (UKZN), Durban 4041, South Africa; Department of Chemical Engineering, Indian Institute of Technology (IIT) Kharagpur, West Bengal, 721302, IndiaThe main aim of the work was to investigate if simple reactor blocks could be combined to adequately represent complex reactor configurations; with the objectives of selecting an appropriate reaction scheme, creating a working simulation and validating the results obtained from the simulation. An ethane cracker reactor is simulated using Aspen Plus, for a molecular reaction scheme, made up of seven reactions and eight hydrocarbon components; using the kinetics and reactor geometrics. Several assumptions were made such that the fired furnace reactor could be modeled as a series of two plug flow reactors using Aspen Plus. Modeling of a fired furnace reactor for the cracking of ethane is made difficult by the inherent separation between the convection and radiation sections; a difficulty which was overcome by separating the convection region and the radiation region of the fired furnace reactor into two simulations such that temperatures were solved for iteratively. A firebox simulation was created with the intent of finding the optimal fuel and air flow rates that would supply the fired furnace rector with the required 2490 kW; these flow rates were found to be 190 kmol hr−1 and 60 kmol hr−1.http://www.sciencedirect.com/science/article/pii/S1026918522001056Fired furnace reactorCrackingHydrocarbonConversionKineticsSimulation |
spellingShingle | Tristan Lee Zebert David Lokhat Swamy Kurella B.C. Meikap Modeling and simulation of ethane cracker reactor using Aspen Plus South African Journal of Chemical Engineering Fired furnace reactor Cracking Hydrocarbon Conversion Kinetics Simulation |
title | Modeling and simulation of ethane cracker reactor using Aspen Plus |
title_full | Modeling and simulation of ethane cracker reactor using Aspen Plus |
title_fullStr | Modeling and simulation of ethane cracker reactor using Aspen Plus |
title_full_unstemmed | Modeling and simulation of ethane cracker reactor using Aspen Plus |
title_short | Modeling and simulation of ethane cracker reactor using Aspen Plus |
title_sort | modeling and simulation of ethane cracker reactor using aspen plus |
topic | Fired furnace reactor Cracking Hydrocarbon Conversion Kinetics Simulation |
url | http://www.sciencedirect.com/science/article/pii/S1026918522001056 |
work_keys_str_mv | AT tristanleezebert modelingandsimulationofethanecrackerreactorusingaspenplus AT davidlokhat modelingandsimulationofethanecrackerreactorusingaspenplus AT swamykurella modelingandsimulationofethanecrackerreactorusingaspenplus AT bcmeikap modelingandsimulationofethanecrackerreactorusingaspenplus |