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Data concerning adsorption equilibria of carbon dioxide, nitrogen and oxygen over a zeolite molecular sieve 13X for the modelling of carbon dioxide capture from gaseous mixtures by adsorptive processes
Experimental adsorption isotherms of carbon dioxide, nitrogen and oxygen at 293, 313 and 333 K over a zeolite molecular sieve 13X Grace are presented. The data were used in the simulations of the hybrid VSA-membrane process for carbon dioxide capture from flue gas as presented in a related article e...
Autores principales: | , , , |
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Formato: | Online Artículo Texto |
Lenguaje: | English |
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Elsevier
2020
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Acceso en línea: | https://www.ncbi.nlm.nih.gov/pmc/articles/PMC7214829/ https://www.ncbi.nlm.nih.gov/pubmed/32420427 http://dx.doi.org/10.1016/j.dib.2020.105638 |
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author | Jaschik, Manfred Tanczyk, Marek Jaschik, Jolanta Janusz-Cygan, Aleksandra |
author_facet | Jaschik, Manfred Tanczyk, Marek Jaschik, Jolanta Janusz-Cygan, Aleksandra |
author_sort | Jaschik, Manfred |
collection | PubMed |
description | Experimental adsorption isotherms of carbon dioxide, nitrogen and oxygen at 293, 313 and 333 K over a zeolite molecular sieve 13X Grace are presented. The data were used in the simulations of the hybrid VSA-membrane process for carbon dioxide capture from flue gas as presented in a related article entitled “The performance of a hybrid VSA-membrane process for the capture of CO(2) from flue gas” [1]. A representative sample of ZSM 13X Grace (149.7 mg) was prepared using the Microscal Spinning Riffler. Adsorption equilibria were determined by a gravimetric method, which uses a microbalance IGA003, Hiden Isochema Ltd., UK at temperatures of 293, 313 and 333 K. Every adsorption isotherm was started at 0 bar. For CO(2) the equilibrium concentration reaches 3.755-4.857 mol kg(−1) at the maximum pressure of 1 bar. In the case of N(2) and O(2) the equilibrium concentration reaches, respectively, 0.721-1.255 mol kg(−1) and 0.299-0.531 mol kg(−1) at the maximum pressure of 5 bar. Data may be reused in any adsorptive CO(2)/N(2)/O(2) separation process which uses ZMS 13X as an adsorbent. |
format | Online Article Text |
id | pubmed-7214829 |
institution | National Center for Biotechnology Information |
language | English |
publishDate | 2020 |
publisher | Elsevier |
record_format | MEDLINE/PubMed |
spelling | pubmed-72148292020-05-15 Data concerning adsorption equilibria of carbon dioxide, nitrogen and oxygen over a zeolite molecular sieve 13X for the modelling of carbon dioxide capture from gaseous mixtures by adsorptive processes Jaschik, Manfred Tanczyk, Marek Jaschik, Jolanta Janusz-Cygan, Aleksandra Data Brief Chemical Engineering Experimental adsorption isotherms of carbon dioxide, nitrogen and oxygen at 293, 313 and 333 K over a zeolite molecular sieve 13X Grace are presented. The data were used in the simulations of the hybrid VSA-membrane process for carbon dioxide capture from flue gas as presented in a related article entitled “The performance of a hybrid VSA-membrane process for the capture of CO(2) from flue gas” [1]. A representative sample of ZSM 13X Grace (149.7 mg) was prepared using the Microscal Spinning Riffler. Adsorption equilibria were determined by a gravimetric method, which uses a microbalance IGA003, Hiden Isochema Ltd., UK at temperatures of 293, 313 and 333 K. Every adsorption isotherm was started at 0 bar. For CO(2) the equilibrium concentration reaches 3.755-4.857 mol kg(−1) at the maximum pressure of 1 bar. In the case of N(2) and O(2) the equilibrium concentration reaches, respectively, 0.721-1.255 mol kg(−1) and 0.299-0.531 mol kg(−1) at the maximum pressure of 5 bar. Data may be reused in any adsorptive CO(2)/N(2)/O(2) separation process which uses ZMS 13X as an adsorbent. Elsevier 2020-04-30 /pmc/articles/PMC7214829/ /pubmed/32420427 http://dx.doi.org/10.1016/j.dib.2020.105638 Text en © 2020 The Author(s) http://creativecommons.org/licenses/by/4.0/ This is an open access article under the CC BY license (http://creativecommons.org/licenses/by/4.0/). |
spellingShingle | Chemical Engineering Jaschik, Manfred Tanczyk, Marek Jaschik, Jolanta Janusz-Cygan, Aleksandra Data concerning adsorption equilibria of carbon dioxide, nitrogen and oxygen over a zeolite molecular sieve 13X for the modelling of carbon dioxide capture from gaseous mixtures by adsorptive processes |
title | Data concerning adsorption equilibria of carbon dioxide, nitrogen and oxygen over a zeolite molecular sieve 13X for the modelling of carbon dioxide capture from gaseous mixtures by adsorptive processes |
title_full | Data concerning adsorption equilibria of carbon dioxide, nitrogen and oxygen over a zeolite molecular sieve 13X for the modelling of carbon dioxide capture from gaseous mixtures by adsorptive processes |
title_fullStr | Data concerning adsorption equilibria of carbon dioxide, nitrogen and oxygen over a zeolite molecular sieve 13X for the modelling of carbon dioxide capture from gaseous mixtures by adsorptive processes |
title_full_unstemmed | Data concerning adsorption equilibria of carbon dioxide, nitrogen and oxygen over a zeolite molecular sieve 13X for the modelling of carbon dioxide capture from gaseous mixtures by adsorptive processes |
title_short | Data concerning adsorption equilibria of carbon dioxide, nitrogen and oxygen over a zeolite molecular sieve 13X for the modelling of carbon dioxide capture from gaseous mixtures by adsorptive processes |
title_sort | data concerning adsorption equilibria of carbon dioxide, nitrogen and oxygen over a zeolite molecular sieve 13x for the modelling of carbon dioxide capture from gaseous mixtures by adsorptive processes |
topic | Chemical Engineering |
url | https://www.ncbi.nlm.nih.gov/pmc/articles/PMC7214829/ https://www.ncbi.nlm.nih.gov/pubmed/32420427 http://dx.doi.org/10.1016/j.dib.2020.105638 |
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