Process Simulation and Cost Evaluation of Carbon Membranes for CO<sub>2</sub> Removal from High-Pressure Natural Gas

Natural gas sweetening is required to remove the acid gas CO<sub>2</sub> to meet gas grid specifications. Membrane technology has a great potential in this application compared to the state-of-the-art amine absorption technology. Carbon membranes are of particular interest due to their h...

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Main Authors: Yunhan Chu, Xuezhong He
Format: Article
Language:English
Published: MDPI AG 2018-11-01
Series:Membranes
Subjects:
Online Access:https://www.mdpi.com/2077-0375/8/4/118
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spelling doaj-cbbad114980d4d8693bcd29059484ec32020-11-24T21:09:01ZengMDPI AGMembranes2077-03752018-11-018411810.3390/membranes8040118membranes8040118Process Simulation and Cost Evaluation of Carbon Membranes for CO<sub>2</sub> Removal from High-Pressure Natural GasYunhan Chu0Xuezhong He1Department of Chemical Engineering, Norwegian University of Science and Technology, NO 7491 Trondheim, NorwayDepartment of Chemical Engineering, Norwegian University of Science and Technology, NO 7491 Trondheim, NorwayNatural gas sweetening is required to remove the acid gas CO<sub>2</sub> to meet gas grid specifications. Membrane technology has a great potential in this application compared to the state-of-the-art amine absorption technology. Carbon membranes are of particular interest due to their high CO<sub>2</sub>/CH<sub>4</sub> selectivity of over 100. In order to document the advantages of carbon membranes for natural gas (NG) sweetening, HYSYS simulation and cost evaluation were conducted in this work. A two-stage carbon membrane process with recycling in the second stage was found to be technically feasible to achieve &gt;98% CH<sub>4</sub> with &lt;2% CH<sub>4</sub> loss. The specific natural gas processing cost of 1.122 &#215; 10<sup>&#8722;2</sup> $/m<sup>3</sup> sweet NG was estimated at a feed pressure of 90 bar, which was significantly dependent on the capital-related cost. Future work on improving carbon membrane performance is required to increase the competitiveness of carbon membranes for natural gas sweetening.https://www.mdpi.com/2077-0375/8/4/118natural gascarbon membranesCO<sub>2</sub> removalprocess simulationcost estimationmethane loss
collection DOAJ
language English
format Article
sources DOAJ
author Yunhan Chu
Xuezhong He
spellingShingle Yunhan Chu
Xuezhong He
Process Simulation and Cost Evaluation of Carbon Membranes for CO<sub>2</sub> Removal from High-Pressure Natural Gas
Membranes
natural gas
carbon membranes
CO<sub>2</sub> removal
process simulation
cost estimation
methane loss
author_facet Yunhan Chu
Xuezhong He
author_sort Yunhan Chu
title Process Simulation and Cost Evaluation of Carbon Membranes for CO<sub>2</sub> Removal from High-Pressure Natural Gas
title_short Process Simulation and Cost Evaluation of Carbon Membranes for CO<sub>2</sub> Removal from High-Pressure Natural Gas
title_full Process Simulation and Cost Evaluation of Carbon Membranes for CO<sub>2</sub> Removal from High-Pressure Natural Gas
title_fullStr Process Simulation and Cost Evaluation of Carbon Membranes for CO<sub>2</sub> Removal from High-Pressure Natural Gas
title_full_unstemmed Process Simulation and Cost Evaluation of Carbon Membranes for CO<sub>2</sub> Removal from High-Pressure Natural Gas
title_sort process simulation and cost evaluation of carbon membranes for co<sub>2</sub> removal from high-pressure natural gas
publisher MDPI AG
series Membranes
issn 2077-0375
publishDate 2018-11-01
description Natural gas sweetening is required to remove the acid gas CO<sub>2</sub> to meet gas grid specifications. Membrane technology has a great potential in this application compared to the state-of-the-art amine absorption technology. Carbon membranes are of particular interest due to their high CO<sub>2</sub>/CH<sub>4</sub> selectivity of over 100. In order to document the advantages of carbon membranes for natural gas (NG) sweetening, HYSYS simulation and cost evaluation were conducted in this work. A two-stage carbon membrane process with recycling in the second stage was found to be technically feasible to achieve &gt;98% CH<sub>4</sub> with &lt;2% CH<sub>4</sub> loss. The specific natural gas processing cost of 1.122 &#215; 10<sup>&#8722;2</sup> $/m<sup>3</sup> sweet NG was estimated at a feed pressure of 90 bar, which was significantly dependent on the capital-related cost. Future work on improving carbon membrane performance is required to increase the competitiveness of carbon membranes for natural gas sweetening.
topic natural gas
carbon membranes
CO<sub>2</sub> removal
process simulation
cost estimation
methane loss
url https://www.mdpi.com/2077-0375/8/4/118
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AT xuezhonghe processsimulationandcostevaluationofcarbonmembranesforcosub2subremovalfromhighpressurenaturalgas
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