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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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 >98% CH<sub>4</sub> with <2% CH<sub>4</sub> loss. The specific natural gas processing cost of 1.122 × 10<sup>−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 >98% CH<sub>4</sub> with <2% CH<sub>4</sub> loss. The specific natural gas processing cost of 1.122 × 10<sup>−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 |
work_keys_str_mv |
AT yunhanchu processsimulationandcostevaluationofcarbonmembranesforcosub2subremovalfromhighpressurenaturalgas AT xuezhonghe processsimulationandcostevaluationofcarbonmembranesforcosub2subremovalfromhighpressurenaturalgas |
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1716758871345725440 |