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Tunable integration of absorption-membrane-adsorption for efficiently separating low boiling gas mixtures near normal temperature

Separation of low boiling gas mixtures is widely concerned in process industries. Now their separations heavily rely upon energy-intensive cryogenic processes. Here, we report a pseudo-absorption process for separating low boiling gas mixtures near normal temperature. In this process, absorption-mem...

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Autores principales: Liu, Huang, Pan, Yong, Liu, Bei, Sun, Changyu, Guo, Ping, Gao, Xueteng, Yang, Lanying, Ma, Qinglan, Chen, Guangjin
Formato: Online Artículo Texto
Lenguaje:English
Publicado: Nature Publishing Group 2016
Materias:
Acceso en línea:https://www.ncbi.nlm.nih.gov/pmc/articles/PMC4759557/
https://www.ncbi.nlm.nih.gov/pubmed/26892255
http://dx.doi.org/10.1038/srep21114
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author Liu, Huang
Pan, Yong
Liu, Bei
Sun, Changyu
Guo, Ping
Gao, Xueteng
Yang, Lanying
Ma, Qinglan
Chen, Guangjin
author_facet Liu, Huang
Pan, Yong
Liu, Bei
Sun, Changyu
Guo, Ping
Gao, Xueteng
Yang, Lanying
Ma, Qinglan
Chen, Guangjin
author_sort Liu, Huang
collection PubMed
description Separation of low boiling gas mixtures is widely concerned in process industries. Now their separations heavily rely upon energy-intensive cryogenic processes. Here, we report a pseudo-absorption process for separating low boiling gas mixtures near normal temperature. In this process, absorption-membrane-adsorption is integrated by suspending suitable porous ZIF material in suitable solvent and forming selectively permeable liquid membrane around ZIF particles. Green solvents like water and glycol were used to form ZIF-8 slurry and tune the permeability of liquid membrane surrounding ZIF-8 particles. We found glycol molecules form tighter membrane while water molecules form looser membrane because of the hydrophobicity of ZIF-8. When using mixing solvents composed of glycol and water, the permeability of liquid membrane becomes tunable. It is shown that ZIF-8/water slurry always manifests remarkable higher separation selectivity than solid ZIF-8 and it could be tuned to further enhance the capture of light hydrocarbons by adding suitable quantity of glycol to water. Because of its lower viscosity and higher sorption/desorption rate, tunable ZIF-8/water-glycol slurry could be readily used as liquid absorbent to separate different kinds of low boiling gas mixtures by applying a multistage separation process in one traditional absorption tower, especially for the capture of light hydrocarbons.
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spelling pubmed-47595572016-02-26 Tunable integration of absorption-membrane-adsorption for efficiently separating low boiling gas mixtures near normal temperature Liu, Huang Pan, Yong Liu, Bei Sun, Changyu Guo, Ping Gao, Xueteng Yang, Lanying Ma, Qinglan Chen, Guangjin Sci Rep Article Separation of low boiling gas mixtures is widely concerned in process industries. Now their separations heavily rely upon energy-intensive cryogenic processes. Here, we report a pseudo-absorption process for separating low boiling gas mixtures near normal temperature. In this process, absorption-membrane-adsorption is integrated by suspending suitable porous ZIF material in suitable solvent and forming selectively permeable liquid membrane around ZIF particles. Green solvents like water and glycol were used to form ZIF-8 slurry and tune the permeability of liquid membrane surrounding ZIF-8 particles. We found glycol molecules form tighter membrane while water molecules form looser membrane because of the hydrophobicity of ZIF-8. When using mixing solvents composed of glycol and water, the permeability of liquid membrane becomes tunable. It is shown that ZIF-8/water slurry always manifests remarkable higher separation selectivity than solid ZIF-8 and it could be tuned to further enhance the capture of light hydrocarbons by adding suitable quantity of glycol to water. Because of its lower viscosity and higher sorption/desorption rate, tunable ZIF-8/water-glycol slurry could be readily used as liquid absorbent to separate different kinds of low boiling gas mixtures by applying a multistage separation process in one traditional absorption tower, especially for the capture of light hydrocarbons. Nature Publishing Group 2016-02-19 /pmc/articles/PMC4759557/ /pubmed/26892255 http://dx.doi.org/10.1038/srep21114 Text en Copyright © 2016, Macmillan Publishers Limited http://creativecommons.org/licenses/by/4.0/ This work is licensed under a Creative Commons Attribution 4.0 International License. The images or other third party material in this article are included in the article’s Creative Commons license, unless indicated otherwise in the credit line; if the material is not included under the Creative Commons license, users will need to obtain permission from the license holder to reproduce the material. To view a copy of this license, visit http://creativecommons.org/licenses/by/4.0/
spellingShingle Article
Liu, Huang
Pan, Yong
Liu, Bei
Sun, Changyu
Guo, Ping
Gao, Xueteng
Yang, Lanying
Ma, Qinglan
Chen, Guangjin
Tunable integration of absorption-membrane-adsorption for efficiently separating low boiling gas mixtures near normal temperature
title Tunable integration of absorption-membrane-adsorption for efficiently separating low boiling gas mixtures near normal temperature
title_full Tunable integration of absorption-membrane-adsorption for efficiently separating low boiling gas mixtures near normal temperature
title_fullStr Tunable integration of absorption-membrane-adsorption for efficiently separating low boiling gas mixtures near normal temperature
title_full_unstemmed Tunable integration of absorption-membrane-adsorption for efficiently separating low boiling gas mixtures near normal temperature
title_short Tunable integration of absorption-membrane-adsorption for efficiently separating low boiling gas mixtures near normal temperature
title_sort tunable integration of absorption-membrane-adsorption for efficiently separating low boiling gas mixtures near normal temperature
topic Article
url https://www.ncbi.nlm.nih.gov/pmc/articles/PMC4759557/
https://www.ncbi.nlm.nih.gov/pubmed/26892255
http://dx.doi.org/10.1038/srep21114
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