Methane Production and Carbon Capture by Hydrate Swapping

There are essentially two different approaches to producing methane from natural gas hydrate reservoirs, either bring the hydrate out of its thermodynamic stability region or expose the hydrate to a substance that will form a more stable hydrate structure, forcing an in situ swapping of the trapped...

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Published in:Energy & Fuels
Main Authors: Mu, Liang, von Solms, Nicolas
Format: Article in Journal/Newspaper
Language:English
Published: 2017
Subjects:
Online Access:https://orbit.dtu.dk/en/publications/d75ea973-56b9-49db-82d3-e442ea170d5f
https://doi.org/10.1021/acs.energyfuels.6b01638
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spelling ftdtupubl:oai:pure.atira.dk:publications/d75ea973-56b9-49db-82d3-e442ea170d5f 2024-06-23T07:54:38+00:00 Methane Production and Carbon Capture by Hydrate Swapping Mu, Liang von Solms, Nicolas 2017 https://orbit.dtu.dk/en/publications/d75ea973-56b9-49db-82d3-e442ea170d5f https://doi.org/10.1021/acs.energyfuels.6b01638 eng eng info:eu-repo/grantAgreement/EC/FP7/609405 https://orbit.dtu.dk/en/publications/d75ea973-56b9-49db-82d3-e442ea170d5f info:eu-repo/semantics/closedAccess Mu , L & von Solms , N 2017 , ' Methane Production and Carbon Capture by Hydrate Swapping ' , Energy & Fuels , vol. 31 , no. 4 , pp. 3338–3347 . https://doi.org/10.1021/acs.energyfuels.6b01638 article 2017 ftdtupubl https://doi.org/10.1021/acs.energyfuels.6b01638 2024-06-04T15:14:17Z There are essentially two different approaches to producing methane from natural gas hydrate reservoirs, either bring the hydrate out of its thermodynamic stability region or expose the hydrate to a substance that will form a more stable hydrate structure, forcing an in situ swapping of the trapped gas molecules in the structural lattice. In this work, we quantitatively investigate the swapping behavior from injection of pure carbon dioxide and the (CO 2 + N 2 ) binary gas mixture through artificial hydrate-bearing sandstone samples by use of a core-flooding experimental apparatus. A total of 13 experimental runs were performed to examine the influence of operating conditions on methane production by CO 2 /(CO 2 + N 2 ) injection in the temperature range of 274.15–277.15 K and 7.039–10.107 MPa pressure. Our results show that the use of the (CO 2 + N 2 ) binary gas mixture is advantageous compared to the use of pure carbon dioxide in swapping methane from its hydrate phase; the methane recovery efficiency in brine water systems is enhanced relative to pure water systems. The replenishment of a fresh (CO 2 + N 2 ) gas mixture into the vapor phase can be considered as an efficient extraction method because 46.32% of methane was displaced from its hydrate phase with the (CO 2 + N 2 ) binary gas mixture after 341.75 h of exposure to the (CO 2 + N 2 ) gas mixture. During the CH 4 –(CO 2 + N 2 ) swapping process, gas chromatography analysis and calculations demonstrated that nitrogen molecules can take the place of some methane in small hydrate cages, as long as the equilibrium formation pressure of (CO2 + N2) binary gas hydrate is below that of methane hydrate, even though adding nitrogen to carbon dioxide reduces the thermodynamic driving force for the formation of a new hydrate. When other conditions are similar, the methane gas recovery efficiency increases with the increase of the driving force for the swapping process. Article in Journal/Newspaper Methane hydrate Technical University of Denmark: DTU Orbit Energy & Fuels 31 4 3338 3347
institution Open Polar
collection Technical University of Denmark: DTU Orbit
op_collection_id ftdtupubl
language English
description There are essentially two different approaches to producing methane from natural gas hydrate reservoirs, either bring the hydrate out of its thermodynamic stability region or expose the hydrate to a substance that will form a more stable hydrate structure, forcing an in situ swapping of the trapped gas molecules in the structural lattice. In this work, we quantitatively investigate the swapping behavior from injection of pure carbon dioxide and the (CO 2 + N 2 ) binary gas mixture through artificial hydrate-bearing sandstone samples by use of a core-flooding experimental apparatus. A total of 13 experimental runs were performed to examine the influence of operating conditions on methane production by CO 2 /(CO 2 + N 2 ) injection in the temperature range of 274.15–277.15 K and 7.039–10.107 MPa pressure. Our results show that the use of the (CO 2 + N 2 ) binary gas mixture is advantageous compared to the use of pure carbon dioxide in swapping methane from its hydrate phase; the methane recovery efficiency in brine water systems is enhanced relative to pure water systems. The replenishment of a fresh (CO 2 + N 2 ) gas mixture into the vapor phase can be considered as an efficient extraction method because 46.32% of methane was displaced from its hydrate phase with the (CO 2 + N 2 ) binary gas mixture after 341.75 h of exposure to the (CO 2 + N 2 ) gas mixture. During the CH 4 –(CO 2 + N 2 ) swapping process, gas chromatography analysis and calculations demonstrated that nitrogen molecules can take the place of some methane in small hydrate cages, as long as the equilibrium formation pressure of (CO2 + N2) binary gas hydrate is below that of methane hydrate, even though adding nitrogen to carbon dioxide reduces the thermodynamic driving force for the formation of a new hydrate. When other conditions are similar, the methane gas recovery efficiency increases with the increase of the driving force for the swapping process.
format Article in Journal/Newspaper
author Mu, Liang
von Solms, Nicolas
spellingShingle Mu, Liang
von Solms, Nicolas
Methane Production and Carbon Capture by Hydrate Swapping
author_facet Mu, Liang
von Solms, Nicolas
author_sort Mu, Liang
title Methane Production and Carbon Capture by Hydrate Swapping
title_short Methane Production and Carbon Capture by Hydrate Swapping
title_full Methane Production and Carbon Capture by Hydrate Swapping
title_fullStr Methane Production and Carbon Capture by Hydrate Swapping
title_full_unstemmed Methane Production and Carbon Capture by Hydrate Swapping
title_sort methane production and carbon capture by hydrate swapping
publishDate 2017
url https://orbit.dtu.dk/en/publications/d75ea973-56b9-49db-82d3-e442ea170d5f
https://doi.org/10.1021/acs.energyfuels.6b01638
genre Methane hydrate
genre_facet Methane hydrate
op_source Mu , L & von Solms , N 2017 , ' Methane Production and Carbon Capture by Hydrate Swapping ' , Energy & Fuels , vol. 31 , no. 4 , pp. 3338–3347 . https://doi.org/10.1021/acs.energyfuels.6b01638
op_relation info:eu-repo/grantAgreement/EC/FP7/609405
https://orbit.dtu.dk/en/publications/d75ea973-56b9-49db-82d3-e442ea170d5f
op_rights info:eu-repo/semantics/closedAccess
op_doi https://doi.org/10.1021/acs.energyfuels.6b01638
container_title Energy & Fuels
container_volume 31
container_issue 4
container_start_page 3338
op_container_end_page 3347
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