Estimation of CO₂ emissions from petroleum refineries based on the total operable capacity for carbon capture applications

Carbon capture and storage processes are sought to play a major role in reducing carbon emissions from large point sources. Petroleum refineries, in particular, produce several streams that are CO2-rich, including fluidized catalytic cracking, steam methane reforming, and natural gas combustion proc...

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Autores principales: Adhish Chandra Saketh Madugula, Darshan Sachde, Susan D. Hovorka, Timothy A. Meckel, Tracy J. Benson
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Lenguaje:EN
Publicado: Elsevier 2021
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Acceso en línea:https://doaj.org/article/8dfa4eb22b614e49b62be209f699ba90
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spelling oai:doaj.org-article:8dfa4eb22b614e49b62be209f699ba902021-11-18T04:52:55ZEstimation of CO₂ emissions from petroleum refineries based on the total operable capacity for carbon capture applications2666-821110.1016/j.ceja.2021.100162https://doaj.org/article/8dfa4eb22b614e49b62be209f699ba902021-11-01T00:00:00Zhttp://www.sciencedirect.com/science/article/pii/S2666821121000788https://doaj.org/toc/2666-8211Carbon capture and storage processes are sought to play a major role in reducing carbon emissions from large point sources. Petroleum refineries, in particular, produce several streams that are CO2-rich, including fluidized catalytic cracking, steam methane reforming, and natural gas combustion processes that generate heat for refinery operations. Of these, stationary combustion processes account for nearly two-thirds of all CO2 generated within a refinery. In this work, a regression analysis was performed to correlate the size and power requirements for the combined capture, compression, and dehydration process dependent upon a refinery's operating capacity. Refinery capacity and CO2 generation data from 128 U.S. refineries were normalized, and a linear regression model was developed. A capture, compression, and dehydration process model was developed using Aspen HYSYS for delivery of CO2 (10–15 wt. % in steam) to pipeline specifications (500 ppm H2O, 15.2 MPa). Predicted CO2 emissions were 0.1 to 7.7 % of actual emissions, depending on whether a refinery had a low, medium, or high carbon emission/capacity ratio.Adhish Chandra Saketh MadugulaDarshan SachdeSusan D. HovorkaTimothy A. MeckelTracy J. BensonElsevierarticleCarbonCaptureCompressionDehydrationRegressionRefineryChemical engineeringTP155-156ENChemical Engineering Journal Advances, Vol 8, Iss , Pp 100162- (2021)
institution DOAJ
collection DOAJ
language EN
topic Carbon
Capture
Compression
Dehydration
Regression
Refinery
Chemical engineering
TP155-156
spellingShingle Carbon
Capture
Compression
Dehydration
Regression
Refinery
Chemical engineering
TP155-156
Adhish Chandra Saketh Madugula
Darshan Sachde
Susan D. Hovorka
Timothy A. Meckel
Tracy J. Benson
Estimation of CO₂ emissions from petroleum refineries based on the total operable capacity for carbon capture applications
description Carbon capture and storage processes are sought to play a major role in reducing carbon emissions from large point sources. Petroleum refineries, in particular, produce several streams that are CO2-rich, including fluidized catalytic cracking, steam methane reforming, and natural gas combustion processes that generate heat for refinery operations. Of these, stationary combustion processes account for nearly two-thirds of all CO2 generated within a refinery. In this work, a regression analysis was performed to correlate the size and power requirements for the combined capture, compression, and dehydration process dependent upon a refinery's operating capacity. Refinery capacity and CO2 generation data from 128 U.S. refineries were normalized, and a linear regression model was developed. A capture, compression, and dehydration process model was developed using Aspen HYSYS for delivery of CO2 (10–15 wt. % in steam) to pipeline specifications (500 ppm H2O, 15.2 MPa). Predicted CO2 emissions were 0.1 to 7.7 % of actual emissions, depending on whether a refinery had a low, medium, or high carbon emission/capacity ratio.
format article
author Adhish Chandra Saketh Madugula
Darshan Sachde
Susan D. Hovorka
Timothy A. Meckel
Tracy J. Benson
author_facet Adhish Chandra Saketh Madugula
Darshan Sachde
Susan D. Hovorka
Timothy A. Meckel
Tracy J. Benson
author_sort Adhish Chandra Saketh Madugula
title Estimation of CO₂ emissions from petroleum refineries based on the total operable capacity for carbon capture applications
title_short Estimation of CO₂ emissions from petroleum refineries based on the total operable capacity for carbon capture applications
title_full Estimation of CO₂ emissions from petroleum refineries based on the total operable capacity for carbon capture applications
title_fullStr Estimation of CO₂ emissions from petroleum refineries based on the total operable capacity for carbon capture applications
title_full_unstemmed Estimation of CO₂ emissions from petroleum refineries based on the total operable capacity for carbon capture applications
title_sort estimation of co₂ emissions from petroleum refineries based on the total operable capacity for carbon capture applications
publisher Elsevier
publishDate 2021
url https://doaj.org/article/8dfa4eb22b614e49b62be209f699ba90
work_keys_str_mv AT adhishchandrasakethmadugula estimationofco2emissionsfrompetroleumrefineriesbasedonthetotaloperablecapacityforcarboncaptureapplications
AT darshansachde estimationofco2emissionsfrompetroleumrefineriesbasedonthetotaloperablecapacityforcarboncaptureapplications
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AT timothyameckel estimationofco2emissionsfrompetroleumrefineriesbasedonthetotaloperablecapacityforcarboncaptureapplications
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