Hydrogen separation and water gas reforming integrated high-pressure hydrogen production system
The utility model relates to a hydrogen separation and water gas reforming integrated high-pressure hydrogen production system. The hydrogen separation and water gas reforming integrated high-pressurehydrogen production system comprises a reformer, a three-phase heat exchange device, a steam trap, a...
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| creator | YUE XIN LI JIAYI ZHOU SI HAN DIFEI JIAO WENCE LYU SHUANGJIANG ZHAO JIJUN |
| description | The utility model relates to a hydrogen separation and water gas reforming integrated high-pressure hydrogen production system. The hydrogen separation and water gas reforming integrated high-pressurehydrogen production system comprises a reformer, a three-phase heat exchange device, a steam trap, a water-cooling heat exchanger, a carbon dioxide liquefaction device and a hydrogen separation and water gas reforming integrated device, the pump pressure of the liquid pump is 18-50 Mpa, and the operating temperature of the water-cooled heat exchanger is 18-30.8 DEG C. The gas in the system is circularly purified, the theoretical yield can reach 100%, and the hydrogen yield is greater than or equal to 95%.
本实用新型涉及氢分离与水煤气重整一体式高压制氢系统，包括重整器、三相换热装置、疏水器、水冷换热器、二氧化碳液化装置以及氢分离与水煤气重整一体式装置；液态泵的泵压为18～50Mpa，所述水冷换热器作业温度在18～30.8℃。实现对系统内的气体进行循环纯化，理论收率可达到100％，实现氢气收率≥95％。 |
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本实用新型涉及氢分离与水煤气重整一体式高压制氢系统，包括重整器、三相换热装置、疏水器、水冷换热器、二氧化碳液化装置以及氢分离与水煤气重整一体式装置；液态泵的泵压为18～50Mpa，所述水冷换热器作业温度在18～30.8℃。实现对系统内的气体进行循环纯化，理论收率可达到100％，实现氢气收率≥95％。</description><language>chi ; eng</language><subject>CHEMISTRY ; COMPOUNDS THEREOF ; INORGANIC CHEMISTRY ; METALLURGY ; NON-METALLIC ELEMENTS</subject><creationdate>2020</creationdate><oa>free_for_read</oa><woscitedreferencessubscribed>false</woscitedreferencessubscribed></display><links><openurl>$$Topenurl_article</openurl><openurlfulltext>$$Topenurlfull_article</openurlfulltext><thumbnail>$$Tsyndetics_thumb_exl</thumbnail><linktohtml>$$Uhttps://worldwide.espacenet.com/publicationDetails/biblio?FT=D&date=20201124&DB=EPODOC&CC=CN&NR=211998801U$$EHTML$$P50$$Gepo$$Hfree_for_read</linktohtml><link.rule.ids>230,308,780,885,25564,76547</link.rule.ids><linktorsrc>$$Uhttps://worldwide.espacenet.com/publicationDetails/biblio?FT=D&date=20201124&DB=EPODOC&CC=CN&NR=211998801U$$EView_record_in_European_Patent_Office$$FView_record_in_$$GEuropean_Patent_Office$$Hfree_for_read</linktorsrc></links><search><creatorcontrib>YUE XIN</creatorcontrib><creatorcontrib>LI JIAYI</creatorcontrib><creatorcontrib>ZHOU SI</creatorcontrib><creatorcontrib>HAN DIFEI</creatorcontrib><creatorcontrib>JIAO WENCE</creatorcontrib><creatorcontrib>LYU SHUANGJIANG</creatorcontrib><creatorcontrib>ZHAO JIJUN</creatorcontrib><title>Hydrogen separation and water gas reforming integrated high-pressure hydrogen production system</title><description>The utility model relates to a hydrogen separation and water gas reforming integrated high-pressure hydrogen production system. The hydrogen separation and water gas reforming integrated high-pressurehydrogen production system comprises a reformer, a three-phase heat exchange device, a steam trap, a water-cooling heat exchanger, a carbon dioxide liquefaction device and a hydrogen separation and water gas reforming integrated device, the pump pressure of the liquid pump is 18-50 Mpa, and the operating temperature of the water-cooled heat exchanger is 18-30.8 DEG C. The gas in the system is circularly purified, the theoretical yield can reach 100%, and the hydrogen yield is greater than or equal to 95%.
本实用新型涉及氢分离与水煤气重整一体式高压制氢系统，包括重整器、三相换热装置、疏水器、水冷换热器、二氧化碳液化装置以及氢分离与水煤气重整一体式装置；液态泵的泵压为18～50Mpa，所述水冷换热器作业温度在18～30.8℃。实现对系统内的气体进行循环纯化，理论收率可达到100％，实现氢气收率≥95％。</description><subject>CHEMISTRY</subject><subject>COMPOUNDS THEREOF</subject><subject>INORGANIC CHEMISTRY</subject><subject>METALLURGY</subject><subject>NON-METALLIC ELEMENTS</subject><fulltext>true</fulltext><rsrctype>patent</rsrctype><creationdate>2020</creationdate><recordtype>patent</recordtype><sourceid>EVB</sourceid><recordid>eNqNzLEKwjAURuEuDqK-w8W9YHVp56J0crJzuTR_00CbhHtTpG-viO5OZ_k426xrViPBwpMisnBywRN7Q09OELKsJBiCzM5bcj7Bvg0Mjc6OeRSoLgIaf5MowSz9Z6KrJsz7bDPwpDh8u8uOt-ujbnLE0EEj9_BIXX0_F0VVleWpaNvLX-gFijc-8Q</recordid><startdate>20201124</startdate><enddate>20201124</enddate><creator>YUE XIN</creator><creator>LI JIAYI</creator><creator>ZHOU SI</creator><creator>HAN DIFEI</creator><creator>JIAO WENCE</creator><creator>LYU SHUANGJIANG</creator><creator>ZHAO JIJUN</creator><scope>EVB</scope></search><sort><creationdate>20201124</creationdate><title>Hydrogen separation and water gas reforming integrated high-pressure hydrogen production system</title><author>YUE XIN ; LI JIAYI ; ZHOU SI ; HAN DIFEI ; JIAO WENCE ; LYU SHUANGJIANG ; ZHAO JIJUN</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-epo_espacenet_CN211998801UU3</frbrgroupid><rsrctype>patents</rsrctype><prefilter>patents</prefilter><language>chi ; eng</language><creationdate>2020</creationdate><topic>CHEMISTRY</topic><topic>COMPOUNDS THEREOF</topic><topic>INORGANIC CHEMISTRY</topic><topic>METALLURGY</topic><topic>NON-METALLIC ELEMENTS</topic><toplevel>online_resources</toplevel><creatorcontrib>YUE XIN</creatorcontrib><creatorcontrib>LI JIAYI</creatorcontrib><creatorcontrib>ZHOU SI</creatorcontrib><creatorcontrib>HAN DIFEI</creatorcontrib><creatorcontrib>JIAO WENCE</creatorcontrib><creatorcontrib>LYU SHUANGJIANG</creatorcontrib><creatorcontrib>ZHAO JIJUN</creatorcontrib><collection>esp@cenet</collection></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext_linktorsrc</fulltext></delivery><addata><au>YUE XIN</au><au>LI JIAYI</au><au>ZHOU SI</au><au>HAN DIFEI</au><au>JIAO WENCE</au><au>LYU SHUANGJIANG</au><au>ZHAO JIJUN</au><format>patent</format><genre>patent</genre><ristype>GEN</ristype><title>Hydrogen separation and water gas reforming integrated high-pressure hydrogen production system</title><date>2020-11-24</date><risdate>2020</risdate><abstract>The utility model relates to a hydrogen separation and water gas reforming integrated high-pressure hydrogen production system. The hydrogen separation and water gas reforming integrated high-pressurehydrogen production system comprises a reformer, a three-phase heat exchange device, a steam trap, a water-cooling heat exchanger, a carbon dioxide liquefaction device and a hydrogen separation and water gas reforming integrated device, the pump pressure of the liquid pump is 18-50 Mpa, and the operating temperature of the water-cooled heat exchanger is 18-30.8 DEG C. The gas in the system is circularly purified, the theoretical yield can reach 100%, and the hydrogen yield is greater than or equal to 95%.
本实用新型涉及氢分离与水煤气重整一体式高压制氢系统，包括重整器、三相换热装置、疏水器、水冷换热器、二氧化碳液化装置以及氢分离与水煤气重整一体式装置；液态泵的泵压为18～50Mpa，所述水冷换热器作业温度在18～30.8℃。实现对系统内的气体进行循环纯化，理论收率可达到100％，实现氢气收率≥95％。</abstract><oa>free_for_read</oa></addata></record> |
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| subjects | CHEMISTRY COMPOUNDS THEREOF INORGANIC CHEMISTRY METALLURGY NON-METALLIC ELEMENTS |
| title | Hydrogen separation and water gas reforming integrated high-pressure hydrogen production system |
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