METHOD FOR XENON SEPARATION FROM GASEOUS MIXTURE
FIELD: cryogenic equipment, particularly for pure xenon production. ^ SUBSTANCE: method involves catalytic burning out hydrocarbons from gaseous mixture; removing moisture and carbon dioxide by sorption process; preliminary cooling and low-temperature rectifying the mixture with obtaining pure xenon...
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creator | KOROBOV A.V GOTOVKO V.L KUZNETSOV A.I KOZIN V.L MIRGOROD I.G KOZLOV S.M MILOVIDOV E.EH KOLESOVA I.P POTAPOV V.N VOLOKITIN L.B FILIPPOV V.M |
description | FIELD: cryogenic equipment, particularly for pure xenon production. ^ SUBSTANCE: method involves catalytic burning out hydrocarbons from gaseous mixture; removing moisture and carbon dioxide by sorption process; preliminary cooling and low-temperature rectifying the mixture with obtaining pure xenon and delivering pure xenon to consumer. Before carrying out catalytic burning out process initial gaseous mixture containing xenon is supplied to catalytic reactor to perform adsorption operation. The catalytic reactor is filled with at least one layer of adsorbent having a capacity for absorbing xenon 8-10 times greater than capacity for absorbing other components of gaseous mixture. Gas mixture composition is continuously determined at catalytic reactor outlet. Gas mixture exiting the catalytic reactor during adsorption process is discharged in atmosphere. Adsorption process is continued up to emergence of xenon in gaseous mixture at catalytic reactor outlet. Then adsorbent is regenerated. During adsorbent regeneration xenon is desorbed along with continuous supplying heat at temperature of 333-353 K. Desorption process is continued up to discontinuance of xenon extraction from adsorbent. Xenon and associated gases extracted from adsorbent during desorption process performing are used to carry out catalytic burning out operation. The obtained xenon has 99.99999% purity degree and the extraction ratio thereof is 0.99. ^ EFFECT: improved xenon purification and increased xenon extraction ratio. ^ 13 cl, 1 dwg |
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Before carrying out catalytic burning out process initial gaseous mixture containing xenon is supplied to catalytic reactor to perform adsorption operation. The catalytic reactor is filled with at least one layer of adsorbent having a capacity for absorbing xenon 8-10 times greater than capacity for absorbing other components of gaseous mixture. Gas mixture composition is continuously determined at catalytic reactor outlet. Gas mixture exiting the catalytic reactor during adsorption process is discharged in atmosphere. Adsorption process is continued up to emergence of xenon in gaseous mixture at catalytic reactor outlet. Then adsorbent is regenerated. During adsorbent regeneration xenon is desorbed along with continuous supplying heat at temperature of 333-353 K. Desorption process is continued up to discontinuance of xenon extraction from adsorbent. Xenon and associated gases extracted from adsorbent during desorption process performing are used to carry out catalytic burning out operation. The obtained xenon has 99.99999% purity degree and the extraction ratio thereof is 0.99. ^ EFFECT: improved xenon purification and increased xenon extraction ratio. ^ 13 cl, 1 dwg</description><edition>7</edition><language>eng ; rus</language><subject>BLASTING ; COMBINED HEATING AND REFRIGERATION SYSTEMS ; HEAT PUMP SYSTEMS ; HEATING ; LIGHTING ; LIQUEFACTION SOLIDIFICATION OF GASES ; LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS ; MANUFACTURE OR STORAGE OF ICE ; MECHANICAL ENGINEERING ; MIXTURES BY PRESSURE AND COLD TREATMENT ; PERFORMING OPERATIONS ; PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL ; REFRIGERATION OR COOLING ; SEPARATION ; TRANSPORTING ; WEAPONS</subject><creationdate>2005</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=20050827&DB=EPODOC&CC=RU&NR=2259522C1$$EHTML$$P50$$Gepo$$Hfree_for_read</linktohtml><link.rule.ids>230,308,780,885,25564,76547</link.rule.ids><linktorsrc>$$Uhttps://worldwide.espacenet.com/publicationDetails/biblio?FT=D&date=20050827&DB=EPODOC&CC=RU&NR=2259522C1$$EView_record_in_European_Patent_Office$$FView_record_in_$$GEuropean_Patent_Office$$Hfree_for_read</linktorsrc></links><search><creatorcontrib>KOROBOV A.V</creatorcontrib><creatorcontrib>GOTOVKO V.L</creatorcontrib><creatorcontrib>KUZNETSOV A.I</creatorcontrib><creatorcontrib>KOZIN V.L</creatorcontrib><creatorcontrib>MIRGOROD I.G</creatorcontrib><creatorcontrib>KOZLOV S.M</creatorcontrib><creatorcontrib>MILOVIDOV E.EH</creatorcontrib><creatorcontrib>KOLESOVA I.P</creatorcontrib><creatorcontrib>POTAPOV V.N</creatorcontrib><creatorcontrib>VOLOKITIN L.B</creatorcontrib><creatorcontrib>FILIPPOV V.M</creatorcontrib><title>METHOD FOR XENON SEPARATION FROM GASEOUS MIXTURE</title><description>FIELD: cryogenic equipment, particularly for pure xenon production. ^ SUBSTANCE: method involves catalytic burning out hydrocarbons from gaseous mixture; removing moisture and carbon dioxide by sorption process; preliminary cooling and low-temperature rectifying the mixture with obtaining pure xenon and delivering pure xenon to consumer. Before carrying out catalytic burning out process initial gaseous mixture containing xenon is supplied to catalytic reactor to perform adsorption operation. The catalytic reactor is filled with at least one layer of adsorbent having a capacity for absorbing xenon 8-10 times greater than capacity for absorbing other components of gaseous mixture. Gas mixture composition is continuously determined at catalytic reactor outlet. Gas mixture exiting the catalytic reactor during adsorption process is discharged in atmosphere. Adsorption process is continued up to emergence of xenon in gaseous mixture at catalytic reactor outlet. Then adsorbent is regenerated. During adsorbent regeneration xenon is desorbed along with continuous supplying heat at temperature of 333-353 K. Desorption process is continued up to discontinuance of xenon extraction from adsorbent. Xenon and associated gases extracted from adsorbent during desorption process performing are used to carry out catalytic burning out operation. The obtained xenon has 99.99999% purity degree and the extraction ratio thereof is 0.99. ^ EFFECT: improved xenon purification and increased xenon extraction ratio. ^ 13 cl, 1 dwg</description><subject>BLASTING</subject><subject>COMBINED HEATING AND REFRIGERATION SYSTEMS</subject><subject>HEAT PUMP SYSTEMS</subject><subject>HEATING</subject><subject>LIGHTING</subject><subject>LIQUEFACTION SOLIDIFICATION OF GASES</subject><subject>LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS</subject><subject>MANUFACTURE OR STORAGE OF ICE</subject><subject>MECHANICAL ENGINEERING</subject><subject>MIXTURES BY PRESSURE AND COLD TREATMENT</subject><subject>PERFORMING OPERATIONS</subject><subject>PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL</subject><subject>REFRIGERATION OR COOLING</subject><subject>SEPARATION</subject><subject>TRANSPORTING</subject><subject>WEAPONS</subject><fulltext>true</fulltext><rsrctype>patent</rsrctype><creationdate>2005</creationdate><recordtype>patent</recordtype><sourceid>EVB</sourceid><recordid>eNrjZDDwdQ3x8HdRcPMPUohw9fP3Uwh2DXAMcgzxBDLdgvx9Fdwdg139Q4MVfD0jQkKDXHkYWNMSc4pTeaE0N4OCm2uIs4duakF-fGpxQWJyal5qSXxQqJGRqaWpkZGzoTERSgD6HSY8</recordid><startdate>20050827</startdate><enddate>20050827</enddate><creator>KOROBOV A.V</creator><creator>GOTOVKO V.L</creator><creator>KUZNETSOV A.I</creator><creator>KOZIN V.L</creator><creator>MIRGOROD I.G</creator><creator>KOZLOV S.M</creator><creator>MILOVIDOV E.EH</creator><creator>KOLESOVA I.P</creator><creator>POTAPOV V.N</creator><creator>VOLOKITIN L.B</creator><creator>FILIPPOV V.M</creator><scope>EVB</scope></search><sort><creationdate>20050827</creationdate><title>METHOD FOR XENON SEPARATION FROM GASEOUS MIXTURE</title><author>KOROBOV A.V ; GOTOVKO V.L ; KUZNETSOV A.I ; KOZIN V.L ; MIRGOROD I.G ; KOZLOV S.M ; MILOVIDOV E.EH ; KOLESOVA I.P ; POTAPOV V.N ; VOLOKITIN L.B ; FILIPPOV V.M</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-epo_espacenet_RU2259522C13</frbrgroupid><rsrctype>patents</rsrctype><prefilter>patents</prefilter><language>eng ; rus</language><creationdate>2005</creationdate><topic>BLASTING</topic><topic>COMBINED HEATING AND REFRIGERATION SYSTEMS</topic><topic>HEAT PUMP SYSTEMS</topic><topic>HEATING</topic><topic>LIGHTING</topic><topic>LIQUEFACTION SOLIDIFICATION OF GASES</topic><topic>LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS</topic><topic>MANUFACTURE OR STORAGE OF ICE</topic><topic>MECHANICAL ENGINEERING</topic><topic>MIXTURES BY PRESSURE AND COLD TREATMENT</topic><topic>PERFORMING OPERATIONS</topic><topic>PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL</topic><topic>REFRIGERATION OR COOLING</topic><topic>SEPARATION</topic><topic>TRANSPORTING</topic><topic>WEAPONS</topic><toplevel>online_resources</toplevel><creatorcontrib>KOROBOV A.V</creatorcontrib><creatorcontrib>GOTOVKO V.L</creatorcontrib><creatorcontrib>KUZNETSOV A.I</creatorcontrib><creatorcontrib>KOZIN V.L</creatorcontrib><creatorcontrib>MIRGOROD I.G</creatorcontrib><creatorcontrib>KOZLOV S.M</creatorcontrib><creatorcontrib>MILOVIDOV E.EH</creatorcontrib><creatorcontrib>KOLESOVA I.P</creatorcontrib><creatorcontrib>POTAPOV V.N</creatorcontrib><creatorcontrib>VOLOKITIN L.B</creatorcontrib><creatorcontrib>FILIPPOV V.M</creatorcontrib><collection>esp@cenet</collection></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext_linktorsrc</fulltext></delivery><addata><au>KOROBOV A.V</au><au>GOTOVKO V.L</au><au>KUZNETSOV A.I</au><au>KOZIN V.L</au><au>MIRGOROD I.G</au><au>KOZLOV S.M</au><au>MILOVIDOV E.EH</au><au>KOLESOVA I.P</au><au>POTAPOV V.N</au><au>VOLOKITIN L.B</au><au>FILIPPOV V.M</au><format>patent</format><genre>patent</genre><ristype>GEN</ristype><title>METHOD FOR XENON SEPARATION FROM GASEOUS MIXTURE</title><date>2005-08-27</date><risdate>2005</risdate><abstract>FIELD: cryogenic equipment, particularly for pure xenon production. ^ SUBSTANCE: method involves catalytic burning out hydrocarbons from gaseous mixture; removing moisture and carbon dioxide by sorption process; preliminary cooling and low-temperature rectifying the mixture with obtaining pure xenon and delivering pure xenon to consumer. Before carrying out catalytic burning out process initial gaseous mixture containing xenon is supplied to catalytic reactor to perform adsorption operation. The catalytic reactor is filled with at least one layer of adsorbent having a capacity for absorbing xenon 8-10 times greater than capacity for absorbing other components of gaseous mixture. Gas mixture composition is continuously determined at catalytic reactor outlet. Gas mixture exiting the catalytic reactor during adsorption process is discharged in atmosphere. Adsorption process is continued up to emergence of xenon in gaseous mixture at catalytic reactor outlet. Then adsorbent is regenerated. During adsorbent regeneration xenon is desorbed along with continuous supplying heat at temperature of 333-353 K. Desorption process is continued up to discontinuance of xenon extraction from adsorbent. Xenon and associated gases extracted from adsorbent during desorption process performing are used to carry out catalytic burning out operation. The obtained xenon has 99.99999% purity degree and the extraction ratio thereof is 0.99. ^ EFFECT: improved xenon purification and increased xenon extraction ratio. ^ 13 cl, 1 dwg</abstract><edition>7</edition><oa>free_for_read</oa></addata></record> |
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subjects | BLASTING COMBINED HEATING AND REFRIGERATION SYSTEMS HEAT PUMP SYSTEMS HEATING LIGHTING LIQUEFACTION SOLIDIFICATION OF GASES LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS MANUFACTURE OR STORAGE OF ICE MECHANICAL ENGINEERING MIXTURES BY PRESSURE AND COLD TREATMENT PERFORMING OPERATIONS PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL REFRIGERATION OR COOLING SEPARATION TRANSPORTING WEAPONS |
title | METHOD FOR XENON SEPARATION FROM GASEOUS MIXTURE |
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