Methane gas hydrate kinetics with mixtures of sodium dodecyl sulphate and tetrabutylammonium bromide
The effect of combining a thermodynamic promoter, tetrabutylammonium bromide (TBAB), with a kinetic promoter, sodium dodecyl sulphate (SDS), to a methane clathrate system was investigated. Kinetic growth experiments were conducted in a semi‐batch stirred tank crystallizer at driving forces of 1500 k...
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crwiley:10.1002/cjce.23094 2024-10-13T14:08:59+00:00 Methane gas hydrate kinetics with mixtures of sodium dodecyl sulphate and tetrabutylammonium bromide Renault‐Crispo, Jean‐Sébastien Servio, Phillip Natural Sciences and Engineering Research Council of Canada 2018 http://dx.doi.org/10.1002/cjce.23094 https://api.wiley.com/onlinelibrary/tdm/v1/articles/10.1002%2Fcjce.23094 https://onlinelibrary.wiley.com/doi/pdf/10.1002/cjce.23094 en eng Wiley http://onlinelibrary.wiley.com/termsAndConditions#vor The Canadian Journal of Chemical Engineering volume 96, issue 7, page 1620-1626 ISSN 0008-4034 1939-019X journal-article 2018 crwiley https://doi.org/10.1002/cjce.23094 2024-09-27T04:16:20Z The effect of combining a thermodynamic promoter, tetrabutylammonium bromide (TBAB), with a kinetic promoter, sodium dodecyl sulphate (SDS), to a methane clathrate system was investigated. Kinetic growth experiments were conducted in a semi‐batch stirred tank crystallizer at driving forces of 1500 kPa using a range of 100 to 1500 ppm SDS and 200 to 200 000 ppm TBAB. Solutions containing low concentrations of TBAB in water reduced methane hydrate growth rates up to 55 % for 1250 ppm TBAB compared to pure water. Solutions containing 900 ppm SDS in water enhanced the growth rate by 880 % compared to pure water. Solutions were then tested combining both promoters. The gradual addition of SDS from concentrations between 100 to 1250 ppm to low‐concentration TBAB systems between 200 to 1250 ppm was initially found to reduce growth kinetics, but eventually increased the growth rates once a threshold SDS concentration was reached. In all cases, the promoting effect of the SDS was more pronounced in the absence of the TBAB. The growth kinetics of systems containing 5 and 20 wt% TBAB also followed a similar inhibition‐promotion trend with the SDS concentration. An increase of 177 % in the gas consumption rate was observed when 1500 ppm SDS was added to the 20 wt% TBAB clathrate system. This work demonstrates that SDS can be added to a TBAB‐water‐methane system to enhance gas consumption rates, but care must be taken to ensure that the concentration of the additives places the system in a promotion regime. Article in Journal/Newspaper Methane hydrate Wiley Online Library The Canadian Journal of Chemical Engineering 96 7 1620 1626 |
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Wiley Online Library |
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crwiley |
language |
English |
description |
The effect of combining a thermodynamic promoter, tetrabutylammonium bromide (TBAB), with a kinetic promoter, sodium dodecyl sulphate (SDS), to a methane clathrate system was investigated. Kinetic growth experiments were conducted in a semi‐batch stirred tank crystallizer at driving forces of 1500 kPa using a range of 100 to 1500 ppm SDS and 200 to 200 000 ppm TBAB. Solutions containing low concentrations of TBAB in water reduced methane hydrate growth rates up to 55 % for 1250 ppm TBAB compared to pure water. Solutions containing 900 ppm SDS in water enhanced the growth rate by 880 % compared to pure water. Solutions were then tested combining both promoters. The gradual addition of SDS from concentrations between 100 to 1250 ppm to low‐concentration TBAB systems between 200 to 1250 ppm was initially found to reduce growth kinetics, but eventually increased the growth rates once a threshold SDS concentration was reached. In all cases, the promoting effect of the SDS was more pronounced in the absence of the TBAB. The growth kinetics of systems containing 5 and 20 wt% TBAB also followed a similar inhibition‐promotion trend with the SDS concentration. An increase of 177 % in the gas consumption rate was observed when 1500 ppm SDS was added to the 20 wt% TBAB clathrate system. This work demonstrates that SDS can be added to a TBAB‐water‐methane system to enhance gas consumption rates, but care must be taken to ensure that the concentration of the additives places the system in a promotion regime. |
author2 |
Natural Sciences and Engineering Research Council of Canada |
format |
Article in Journal/Newspaper |
author |
Renault‐Crispo, Jean‐Sébastien Servio, Phillip |
spellingShingle |
Renault‐Crispo, Jean‐Sébastien Servio, Phillip Methane gas hydrate kinetics with mixtures of sodium dodecyl sulphate and tetrabutylammonium bromide |
author_facet |
Renault‐Crispo, Jean‐Sébastien Servio, Phillip |
author_sort |
Renault‐Crispo, Jean‐Sébastien |
title |
Methane gas hydrate kinetics with mixtures of sodium dodecyl sulphate and tetrabutylammonium bromide |
title_short |
Methane gas hydrate kinetics with mixtures of sodium dodecyl sulphate and tetrabutylammonium bromide |
title_full |
Methane gas hydrate kinetics with mixtures of sodium dodecyl sulphate and tetrabutylammonium bromide |
title_fullStr |
Methane gas hydrate kinetics with mixtures of sodium dodecyl sulphate and tetrabutylammonium bromide |
title_full_unstemmed |
Methane gas hydrate kinetics with mixtures of sodium dodecyl sulphate and tetrabutylammonium bromide |
title_sort |
methane gas hydrate kinetics with mixtures of sodium dodecyl sulphate and tetrabutylammonium bromide |
publisher |
Wiley |
publishDate |
2018 |
url |
http://dx.doi.org/10.1002/cjce.23094 https://api.wiley.com/onlinelibrary/tdm/v1/articles/10.1002%2Fcjce.23094 https://onlinelibrary.wiley.com/doi/pdf/10.1002/cjce.23094 |
genre |
Methane hydrate |
genre_facet |
Methane hydrate |
op_source |
The Canadian Journal of Chemical Engineering volume 96, issue 7, page 1620-1626 ISSN 0008-4034 1939-019X |
op_rights |
http://onlinelibrary.wiley.com/termsAndConditions#vor |
op_doi |
https://doi.org/10.1002/cjce.23094 |
container_title |
The Canadian Journal of Chemical Engineering |
container_volume |
96 |
container_issue |
7 |
container_start_page |
1620 |
op_container_end_page |
1626 |
_version_ |
1812815779887841280 |