Impact of impurities from oxy-fuel CO2 streams on compression strategies for carbon capture and sequestration

The efficacy of Carbon Capture and Sequestration (CCS) as a means to mitigate the CO2 gas emissions from industrial sectors, including fossil fuel operated power stations, requires the minimisation of the costs associated with compression and transportation of the captured CO2. CO2 compression share...

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Main Authors:	Nor Khonisah, Daud, N., Nasuha, S., Martynov, H., Mahgerefteh
Format:	Conference or Workshop Item
Language:	English English
Published:	2019
Subjects:	TP Chemical technology
Online Access:	http://umpir.ump.edu.my/id/eprint/26722/ http://umpir.ump.edu.my/id/eprint/26722/1/58.%20Impact%20of%20impurities%20from%20oxy-fuel%20CO2.pdf http://umpir.ump.edu.my/id/eprint/26722/2/58.1%20Impact%20of%20impurities%20from%20oxy-fuel%20CO2.pdf

id	ump-26722
recordtype	eprints
spelling	ump-267222020-02-13T06:34:10Z http://umpir.ump.edu.my/id/eprint/26722/ Impact of impurities from oxy-fuel CO2 streams on compression strategies for carbon capture and sequestration Nor Khonisah, Daud N., Nasuha S., Martynov H., Mahgerefteh TP Chemical technology The efficacy of Carbon Capture and Sequestration (CCS) as a means to mitigate the CO2 gas emissions from industrial sectors, including fossil fuel operated power stations, requires the minimisation of the costs associated with compression and transportation of the captured CO2. CO2 compression shares a large portion of the costs and energy penalties induced by CCS. The main purpose of this study is to identify the optimum multistage compression strategies for minimising the compression and intercooler power requirements for pure CO2 feed stream. An analytical model based on thermodynamics principles is developed employing Plato Silverfrost FTN95 software and applied to determine the power requirements for various compression strategies and inter-stage cooling duties for CO2 stream compressed from a gaseous state at 1.5 bar and 38 oC to the dense-phase fluid at 151 bar. Compression options examined include conventional multistage integrally geared centrifugal compressors (option A), advanced supersonic shockwave compressors (option B) and multistage compression combined with subcritical (option C) and supercritical liquefaction (option D) and pumping. In each case, the compression power requirement is calculated numerically using a 15-point Gauss-Kronrod quadrature rule in QUADPACK library, and employing the Peng-Robinson Equation of State (PR EOS) implemented in REFPROP v.9.1 to predict the pertinent thermodynamic properties of the CO2. In the case of determining the power demand for inter-stage cooling and liquefaction, a thermodynamic model based on Carnot refrigeration cycle is applied. From the previous study by Witkowski et al., (2013), the power demand for inter-stage cooling duty was assumed neglected. However, based on the present study, the inter-stage cooling duty is predicted to be significantly higher and contributes approximately 30 % from the total power requirement for compression options A, C and D, while reaches 58 % when applied to option B. It is also found that multistage compression combined with subcritical liquefaction using utility streams and subsequent pumping can offer higher efficiency than other compression strategies, while supercritical liquefaction efficiency is only marginally higher than that in the conventional integrally geared centrifugal compression. 2019 Conference or Workshop Item PeerReviewed pdf en http://umpir.ump.edu.my/id/eprint/26722/1/58.%20Impact%20of%20impurities%20from%20oxy-fuel%20CO2.pdf pdf en http://umpir.ump.edu.my/id/eprint/26722/2/58.1%20Impact%20of%20impurities%20from%20oxy-fuel%20CO2.pdf Nor Khonisah, Daud and N., Nasuha and S., Martynov and H., Mahgerefteh (2019) Impact of impurities from oxy-fuel CO2 streams on compression strategies for carbon capture and sequestration. In: 1st Process Systems Engineering & Safety (PROSES) Symposium 2019, 4 September 2019 , Vistana Hotel, Kuantan. pp. 1-8.. (Unpublished)
repository_type	Digital Repository
institution_category	Local University
institution	Universiti Malaysia Pahang
building	UMP Institutional Repository
collection	Online Access
language	English English
topic	TP Chemical technology
spellingShingle	TP Chemical technology Nor Khonisah, Daud N., Nasuha S., Martynov H., Mahgerefteh Impact of impurities from oxy-fuel CO2 streams on compression strategies for carbon capture and sequestration
description	The efficacy of Carbon Capture and Sequestration (CCS) as a means to mitigate the CO2 gas emissions from industrial sectors, including fossil fuel operated power stations, requires the minimisation of the costs associated with compression and transportation of the captured CO2. CO2 compression shares a large portion of the costs and energy penalties induced by CCS. The main purpose of this study is to identify the optimum multistage compression strategies for minimising the compression and intercooler power requirements for pure CO2 feed stream. An analytical model based on thermodynamics principles is developed employing Plato Silverfrost FTN95 software and applied to determine the power requirements for various compression strategies and inter-stage cooling duties for CO2 stream compressed from a gaseous state at 1.5 bar and 38 oC to the dense-phase fluid at 151 bar. Compression options examined include conventional multistage integrally geared centrifugal compressors (option A), advanced supersonic shockwave compressors (option B) and multistage compression combined with subcritical (option C) and supercritical liquefaction (option D) and pumping. In each case, the compression power requirement is calculated numerically using a 15-point Gauss-Kronrod quadrature rule in QUADPACK library, and employing the Peng-Robinson Equation of State (PR EOS) implemented in REFPROP v.9.1 to predict the pertinent thermodynamic properties of the CO2. In the case of determining the power demand for inter-stage cooling and liquefaction, a thermodynamic model based on Carnot refrigeration cycle is applied. From the previous study by Witkowski et al., (2013), the power demand for inter-stage cooling duty was assumed neglected. However, based on the present study, the inter-stage cooling duty is predicted to be significantly higher and contributes approximately 30 % from the total power requirement for compression options A, C and D, while reaches 58 % when applied to option B. It is also found that multistage compression combined with subcritical liquefaction using utility streams and subsequent pumping can offer higher efficiency than other compression strategies, while supercritical liquefaction efficiency is only marginally higher than that in the conventional integrally geared centrifugal compression.
format	Conference or Workshop Item
author	Nor Khonisah, Daud N., Nasuha S., Martynov H., Mahgerefteh
author_facet	Nor Khonisah, Daud N., Nasuha S., Martynov H., Mahgerefteh
author_sort	Nor Khonisah, Daud
title	Impact of impurities from oxy-fuel CO2 streams on compression strategies for carbon capture and sequestration
title_short	Impact of impurities from oxy-fuel CO2 streams on compression strategies for carbon capture and sequestration
title_full	Impact of impurities from oxy-fuel CO2 streams on compression strategies for carbon capture and sequestration
title_fullStr	Impact of impurities from oxy-fuel CO2 streams on compression strategies for carbon capture and sequestration
title_full_unstemmed	Impact of impurities from oxy-fuel CO2 streams on compression strategies for carbon capture and sequestration
title_sort	impact of impurities from oxy-fuel co2 streams on compression strategies for carbon capture and sequestration
publishDate	2019
url	http://umpir.ump.edu.my/id/eprint/26722/ http://umpir.ump.edu.my/id/eprint/26722/1/58.%20Impact%20of%20impurities%20from%20oxy-fuel%20CO2.pdf http://umpir.ump.edu.my/id/eprint/26722/2/58.1%20Impact%20of%20impurities%20from%20oxy-fuel%20CO2.pdf
first_indexed	2023-09-18T22:41:47Z
last_indexed	2023-09-18T22:41:47Z
_version_	1777416963006398464

Impact of impurities from oxy-fuel CO2 streams on compression strategies for carbon capture and sequestration

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