Separation dynamics of hydrogen isotope gas in mesoporous and microporous adsorbent beds at 77 K: SBA-15 and zeolites 5A, Y, 10X

The separation of a hydrogen isotope mixture on porous materials was studied using equilibrium and breakthrough experiments. The adsorption equilibria of H2 and D2 on SBA-15 with mesopores and molecular sieves 5A, Y, and 10X with micropores were measured at 77 K using the volumetric method. The brea...

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Veröffentlicht in:International journal of hydrogen energy 2014-03, Vol.39 (9), p.4437-4446
Hauptverfasser: Chu, Xiao-Zhong, Cheng, Zhi-Peng, Xiang, Xin-Xin, Xu, Ji-Ming, Zhao, Yi-Jiang, Zhang, Wei-Guang, Lv, Jin-Shun, Zhou, Ya-Ping, Zhou, Li, Moon, Dong-Kyu, Lee, Chang-Ha
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container_issue 9
container_start_page 4437
container_title International journal of hydrogen energy
container_volume 39
creator Chu, Xiao-Zhong
Cheng, Zhi-Peng
Xiang, Xin-Xin
Xu, Ji-Ming
Zhao, Yi-Jiang
Zhang, Wei-Guang
Lv, Jin-Shun
Zhou, Ya-Ping
Zhou, Li
Moon, Dong-Kyu
Lee, Chang-Ha
description The separation of a hydrogen isotope mixture on porous materials was studied using equilibrium and breakthrough experiments. The adsorption equilibria of H2 and D2 on SBA-15 with mesopores and molecular sieves 5A, Y, and 10X with micropores were measured at 77 K using the volumetric method. The breakthrough experiments of a H2 and D2 mixture in each adsorbent bed were carried out at various conditions of flow rate and pressure. The equilibrium ratio of D2 to H2 on mesoporous molecular sieves was larger than the ratio on microporous molecular sieves (SBA-15 > 10X > Y > 5A), but the difference among the adsorbents decreased with increases in pressure. On the other hand, the order of breakthrough separation factor showed the opposite result (SBA-15 
doi_str_mv 10.1016/j.ijhydene.2014.01.031
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The adsorption equilibria of H2 and D2 on SBA-15 with mesopores and molecular sieves 5A, Y, and 10X with micropores were measured at 77 K using the volumetric method. The breakthrough experiments of a H2 and D2 mixture in each adsorbent bed were carried out at various conditions of flow rate and pressure. The equilibrium ratio of D2 to H2 on mesoporous molecular sieves was larger than the ratio on microporous molecular sieves (SBA-15 > 10X > Y > 5A), but the difference among the adsorbents decreased with increases in pressure. On the other hand, the order of breakthrough separation factor showed the opposite result (SBA-15 < 10X < Y < 5A). The breakthrough separation factors for zeolite 10X was approximately equal to the equilibrium ratio of D2 to H2 at the corresponding partial pressures, whereas zeolites 5A and Y showed higher breakthrough separation factors than their equilibrium ratios. In SBA-15, the separation factors from breakthrough results were even smaller than the corresponding equilibrium ratio. In the microporous adsorbent with a limited pore size (zeolite 5A in the study), the diffusion mechanism contributed to the separation of hydrogen isotope gases as one of key factors. •Separation of hydrogen isotope at 77 K was studied on SBA-15 and zeolites 5A, Y, 10X.•Separation factor (SBA-15 < 10X < Y < 5A) and equilibrium ratio were in reverse order.•Dynamic effect contributed to the separation of hydrogen isotope in zeolite 5A.•The adsorption equilibrium difference dominated the separation in zeolite 10X.•Dynamic effect of hydrogen isotope separation decreased with increasing pore size.]]></description><identifier>ISSN: 0360-3199</identifier><identifier>EISSN: 1879-3487</identifier><identifier>DOI: 10.1016/j.ijhydene.2014.01.031</identifier><identifier>CODEN: IJHEDX</identifier><language>eng</language><publisher>Kidlington: Elsevier Ltd</publisher><subject>Adsorbents ; Adsorption ; Alternative fuels. 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The adsorption equilibria of H2 and D2 on SBA-15 with mesopores and molecular sieves 5A, Y, and 10X with micropores were measured at 77 K using the volumetric method. The breakthrough experiments of a H2 and D2 mixture in each adsorbent bed were carried out at various conditions of flow rate and pressure. The equilibrium ratio of D2 to H2 on mesoporous molecular sieves was larger than the ratio on microporous molecular sieves (SBA-15 > 10X > Y > 5A), but the difference among the adsorbents decreased with increases in pressure. On the other hand, the order of breakthrough separation factor showed the opposite result (SBA-15 < 10X < Y < 5A). The breakthrough separation factors for zeolite 10X was approximately equal to the equilibrium ratio of D2 to H2 at the corresponding partial pressures, whereas zeolites 5A and Y showed higher breakthrough separation factors than their equilibrium ratios. 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Production and utilization</subject><subject>Applied sciences</subject><subject>Diffusion</subject><subject>Energy</subject><subject>Exact sciences and technology</subject><subject>Fuels</subject><subject>Hydrogen</subject><subject>Hydrogen isotope</subject><subject>Hydrogen isotopes</subject><subject>Hydrogen-based energy</subject><subject>Molecular sieve</subject><subject>Molecular sieves</subject><subject>Porous materials</subject><subject>Separation</subject><subject>Separation mechanism</subject><subject>Zeolites</subject><issn>0360-3199</issn><issn>1879-3487</issn><fulltext>true</fulltext><rsrctype>article</rsrctype><creationdate>2014</creationdate><recordtype>article</recordtype><recordid>eNqFkE1uFDEQhS0EEkPgCsgbJBbpxtV2t9usGCL-RCQWAQlWltsuB4967MbuIA07bsJZOBkOE7JlVXrS9-pVPUIeA2uBwfBs14bd14PDiG3HQLQMWsbhDtnAKFXDxSjvkg3jA2s4KHWfPChlxxhIJtSG_LzAxWSzhhSpO0SzD7bQ5GldmNMlRhpKWtOC9NIUGiLdY0lLyumqUBMdrXi-1a6kPGFc6YSuypVK-fvX--f04uW2gf4v_wPTHFYstN-e0i-nFNjnh-SeN3PBRzfzhHx6_erj2dvm_MObd2fb88YK6NZm9KLjkk8SmPdccD_JEYzqJR87NqoRwTvwXg4KfCe8MK7vJ6esst6JyXb8hDw97l1y-naFZdX7UCzOs4lYz9fQc6i9MTZUdDii9blSMnq95LA3-aCB6evO9U7_61xfd64Z6Oqtxic3GaZYM_tsog3l1t2NvK_Hysq9OHJYH_4eMOtiA0aLLmS0q3Yp_C_qD7F5mvA</recordid><startdate>20140318</startdate><enddate>20140318</enddate><creator>Chu, Xiao-Zhong</creator><creator>Cheng, Zhi-Peng</creator><creator>Xiang, Xin-Xin</creator><creator>Xu, Ji-Ming</creator><creator>Zhao, Yi-Jiang</creator><creator>Zhang, Wei-Guang</creator><creator>Lv, Jin-Shun</creator><creator>Zhou, Ya-Ping</creator><creator>Zhou, Li</creator><creator>Moon, Dong-Kyu</creator><creator>Lee, Chang-Ha</creator><general>Elsevier Ltd</general><general>Elsevier</general><scope>IQODW</scope><scope>AAYXX</scope><scope>CITATION</scope><scope>7SP</scope><scope>7SR</scope><scope>8FD</scope><scope>JG9</scope><scope>L7M</scope></search><sort><creationdate>20140318</creationdate><title>Separation dynamics of hydrogen isotope gas in mesoporous and microporous adsorbent beds at 77 K: SBA-15 and zeolites 5A, Y, 10X</title><author>Chu, Xiao-Zhong ; Cheng, Zhi-Peng ; Xiang, Xin-Xin ; Xu, Ji-Ming ; Zhao, Yi-Jiang ; Zhang, Wei-Guang ; Lv, Jin-Shun ; Zhou, Ya-Ping ; Zhou, Li ; Moon, Dong-Kyu ; Lee, Chang-Ha</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-LOGICAL-c412t-8f42373b710ff343fb781a9573820898e1fd1ff7691f24f4ad55bd9c9cfd4bc23</frbrgroupid><rsrctype>articles</rsrctype><prefilter>articles</prefilter><language>eng</language><creationdate>2014</creationdate><topic>Adsorbents</topic><topic>Adsorption</topic><topic>Alternative fuels. 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The adsorption equilibria of H2 and D2 on SBA-15 with mesopores and molecular sieves 5A, Y, and 10X with micropores were measured at 77 K using the volumetric method. The breakthrough experiments of a H2 and D2 mixture in each adsorbent bed were carried out at various conditions of flow rate and pressure. The equilibrium ratio of D2 to H2 on mesoporous molecular sieves was larger than the ratio on microporous molecular sieves (SBA-15 > 10X > Y > 5A), but the difference among the adsorbents decreased with increases in pressure. On the other hand, the order of breakthrough separation factor showed the opposite result (SBA-15 < 10X < Y < 5A). The breakthrough separation factors for zeolite 10X was approximately equal to the equilibrium ratio of D2 to H2 at the corresponding partial pressures, whereas zeolites 5A and Y showed higher breakthrough separation factors than their equilibrium ratios. In SBA-15, the separation factors from breakthrough results were even smaller than the corresponding equilibrium ratio. In the microporous adsorbent with a limited pore size (zeolite 5A in the study), the diffusion mechanism contributed to the separation of hydrogen isotope gases as one of key factors. •Separation of hydrogen isotope at 77 K was studied on SBA-15 and zeolites 5A, Y, 10X.•Separation factor (SBA-15 < 10X < Y < 5A) and equilibrium ratio were in reverse order.•Dynamic effect contributed to the separation of hydrogen isotope in zeolite 5A.•The adsorption equilibrium difference dominated the separation in zeolite 10X.•Dynamic effect of hydrogen isotope separation decreased with increasing pore size.]]></abstract><cop>Kidlington</cop><pub>Elsevier Ltd</pub><doi>10.1016/j.ijhydene.2014.01.031</doi><tpages>10</tpages></addata></record>
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source Elsevier ScienceDirect Journals
subjects Adsorbents
Adsorption
Alternative fuels. Production and utilization
Applied sciences
Diffusion
Energy
Exact sciences and technology
Fuels
Hydrogen
Hydrogen isotope
Hydrogen isotopes
Hydrogen-based energy
Molecular sieve
Molecular sieves
Porous materials
Separation
Separation mechanism
Zeolites
title Separation dynamics of hydrogen isotope gas in mesoporous and microporous adsorbent beds at 77 K: SBA-15 and zeolites 5A, Y, 10X
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