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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...

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Autores principales: Jaschik, Manfred, Tanczyk, Marek, Jaschik, Jolanta, Janusz-Cygan, Aleksandra
Formato: Online Artículo Texto
Lenguaje:English
Publicado: Elsevier 2020
Materias:
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.
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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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