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The objective of the present study is to assess the potential usefulness of membrane separation processes for removing CO{sub 2} and H{sub 2}S from low-quality natural gas containing substantial amounts of both these ''acid'' gases, e.g., up to 40 mole-% CO{sub 2} and 10 mole-% H{sub 2}S. The membrane processes must be capable of upgrading the crude natural gas to pipeline specifications ({le} 2 mole-% CO{sub 2}, {le} 4 ppm H{sub 2}S). Moreover, these processes must also be economically competitive with the conventional separation techniques, such as gas absorption, utilized for this purpose by the gas industry. | The objective of the present study is to assess the potential usefulness of membrane separation processes for removing CO{sub 2} and H{sub 2}S from low-quality natural gas containing substantial amounts of both these ''acid'' gases, e.g., up to 40 mole-% CO{sub 2} and 10 mole-% H{sub 2}S. The membrane processes must be capable of upgrading the crude natural gas to pipeline specifications ({le} 2 mole-% CO{sub 2}, {le} 4 ppm H{sub 2}S). Moreover, these processes must also be economically competitive with the conventional separation techniques, such as gas absorption, utilized for this purpose by the gas industry. | ||
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* [https://digital.library.unt.edu/ark:/67531/metadc786004/m2/1/high_res_d/834349.pdf https://digital.library.unt.edu/ark:/67531/metadc786004/m2/1/high_res_d/834349.pdf] | * [https://digital.library.unt.edu/ark:/67531/metadc786004/m2/1/high_res_d/834349.pdf https://digital.library.unt.edu/ark:/67531/metadc786004/m2/1/high_res_d/834349.pdf] | ||
| − | * [https://core.ac.uk/display/71225861 https://core.ac.uk/display/71225861],[https://digital.library.unt.edu/ark:/67531/metadc786004/m2/1/high_res_d/834349.pdf https://digital.library.unt.edu/ark:/67531/metadc786004/m2/1/high_res_d/834349.pdf],[https://digital.library.unt.edu/ark:/67531/metadc786004 https://digital.library.unt.edu/ark:/67531/metadc786004],[https://academic.microsoft.com/#/detail/1548897900 https://academic.microsoft.com/#/detail/1548897900] | + | * [https://core.ac.uk/display/71225861 https://core.ac.uk/display/71225861], |
| + | : [https://digital.library.unt.edu/ark:/67531/metadc786004/m2/1/high_res_d/834349.pdf https://digital.library.unt.edu/ark:/67531/metadc786004/m2/1/high_res_d/834349.pdf], | ||
| + | : [https://www.scipedia.com/public/S.A.Stern_et_al_2000a https://www.scipedia.com/public/S.A.Stern_et_al_2000a], | ||
| + | : [https://digital.library.unt.edu/ark:/67531/metadc786004 https://digital.library.unt.edu/ark:/67531/metadc786004], | ||
| + | : [http://www.osti.gov/scitech/biblio/834349-upgrading-natural-gas-via-membrane-separation-processes http://www.osti.gov/scitech/biblio/834349-upgrading-natural-gas-via-membrane-separation-processes], | ||
| + | : [https://academic.microsoft.com/#/detail/1548897900 https://academic.microsoft.com/#/detail/1548897900] | ||
Latest revision as of 12:42, 22 January 2021
Abstract
The objective of the present study is to assess the potential usefulness of membrane separation processes for removing CO{sub 2} and H{sub 2}S from low-quality natural gas containing substantial amounts of both these acid gases, e.g., up to 40 mole-% CO{sub 2} and 10 mole-% H{sub 2}S. The membrane processes must be capable of upgrading the crude natural gas to pipeline specifications ({le} 2 mole-% CO{sub 2}, {le} 4 ppm H{sub 2}S). Moreover, these processes must also be economically competitive with the conventional separation techniques, such as gas absorption, utilized for this purpose by the gas industry.
Original document
The different versions of the original document can be found in:
- https://digital.library.unt.edu/ark:/67531/metadc786004/m2/1/high_res_d/834349.pdf,
- https://www.scipedia.com/public/S.A.Stern_et_al_2000a,
- https://digital.library.unt.edu/ark:/67531/metadc786004,
- http://www.osti.gov/scitech/biblio/834349-upgrading-natural-gas-via-membrane-separation-processes,
- https://academic.microsoft.com/#/detail/1548897900
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Document information
Published on 01/01/2000
Volume 2000, 2000
DOI: 10.2172/834349
Licence: CC BY-NC-SA license
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