CATALYST FOR CORBON MONOXIDE CONVERSION IN SOUR GAS
A sulphactive CO conversion catalyst comprises(a) an aluminous catalyst carrier; (b) a catalytically active metal compd. from Co or Ni oxide or sulphide or an oxide or sulphide of Gp.(V), (VI), or (VII) transition element; (c) a promotional amt. alkali metal compd., pref. K2CO3; and (d) a promotiona...
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| creator | MERRIAM JAY S HOGG CECIL B |
| description | A sulphactive CO conversion catalyst comprises(a) an aluminous catalyst carrier; (b) a catalytically active metal compd. from Co or Ni oxide or sulphide or an oxide or sulphide of Gp.(V), (VI), or (VII) transition element; (c) a promotional amt. alkali metal compd., pref. K2CO3; and (d) a promotional amt. oxide or sulphide of fourth period metal at number 22-25 inclusive, pref. Mn as less than 5 wt.%, expressed as the oxide. CO is catalytically converted with steam to form H2 and CO2, by passing a synthesis gas mixt. of CO and steam, over the catalyst, at 150-540 deg.C but above the dew point of the sybthesis gas mixt.; and at pressure below the dew point pressure of the gas mixt. |
| format | Patent |
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K2CO3; and (d) a promotional amt. oxide or sulphide of fourth period metal at number 22-25 inclusive, pref. Mn as less than 5 wt.%, expressed as the oxide. CO is catalytically converted with steam to form H2 and CO2, by passing a synthesis gas mixt. of CO and steam, over the catalyst, at 150-540 deg.C but above the dew point of the sybthesis gas mixt.; and at pressure below the dew point pressure of the gas mixt.</description><edition>4</edition><language>eng</language><subject>CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOIDCHEMISTRY ; CHEMISTRY ; COMPOUNDS THEREOF ; INORGANIC CHEMISTRY ; METALLURGY ; NON-METALLIC ELEMENTS ; PERFORMING OPERATIONS ; PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL ; THEIR RELEVANT APPARATUS ; TRANSPORTING</subject><creationdate>1987</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=19870926&DB=EPODOC&CC=KR&NR=870001732B1$$EHTML$$P50$$Gepo$$Hfree_for_read</linktohtml><link.rule.ids>230,308,776,881,25543,76293</link.rule.ids><linktorsrc>$$Uhttps://worldwide.espacenet.com/publicationDetails/biblio?FT=D&date=19870926&DB=EPODOC&CC=KR&NR=870001732B1$$EView_record_in_European_Patent_Office$$FView_record_in_$$GEuropean_Patent_Office$$Hfree_for_read</linktorsrc></links><search><creatorcontrib>MERRIAM JAY S</creatorcontrib><creatorcontrib>HOGG CECIL B</creatorcontrib><title>CATALYST FOR CORBON MONOXIDE CONVERSION IN SOUR GAS</title><description>A sulphactive CO conversion catalyst comprises(a) an aluminous catalyst carrier; (b) a catalytically active metal compd. from Co or Ni oxide or sulphide or an oxide or sulphide of Gp.(V), (VI), or (VII) transition element; (c) a promotional amt. alkali metal compd., pref. K2CO3; and (d) a promotional amt. oxide or sulphide of fourth period metal at number 22-25 inclusive, pref. Mn as less than 5 wt.%, expressed as the oxide. CO is catalytically converted with steam to form H2 and CO2, by passing a synthesis gas mixt. of CO and steam, over the catalyst, at 150-540 deg.C but above the dew point of the sybthesis gas mixt.; and at pressure below the dew point pressure of the gas mixt.</description><subject>CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOIDCHEMISTRY</subject><subject>CHEMISTRY</subject><subject>COMPOUNDS THEREOF</subject><subject>INORGANIC CHEMISTRY</subject><subject>METALLURGY</subject><subject>NON-METALLIC ELEMENTS</subject><subject>PERFORMING OPERATIONS</subject><subject>PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL</subject><subject>THEIR RELEVANT APPARATUS</subject><subject>TRANSPORTING</subject><fulltext>true</fulltext><rsrctype>patent</rsrctype><creationdate>1987</creationdate><recordtype>patent</recordtype><sourceid>EVB</sourceid><recordid>eNrjZDB2dgxx9IkMDlFw8w9ScPYPcvL3U_D19_OP8HRxBfL9wlyDgj2BYp5-CsH-oUEK7o7BPAysaYk5xam8UJqbQdnNNcTZQze1ID8-tbggMTk1L7Uk3jvIwtzAwMDQ3NjIycnQmDhVAEl4KCk</recordid><startdate>19870926</startdate><enddate>19870926</enddate><creator>MERRIAM JAY S</creator><creator>HOGG CECIL B</creator><scope>EVB</scope></search><sort><creationdate>19870926</creationdate><title>CATALYST FOR CORBON MONOXIDE CONVERSION IN SOUR GAS</title><author>MERRIAM JAY S ; HOGG CECIL B</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-epo_espacenet_KR870001732BB13</frbrgroupid><rsrctype>patents</rsrctype><prefilter>patents</prefilter><language>eng</language><creationdate>1987</creationdate><topic>CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOIDCHEMISTRY</topic><topic>CHEMISTRY</topic><topic>COMPOUNDS THEREOF</topic><topic>INORGANIC CHEMISTRY</topic><topic>METALLURGY</topic><topic>NON-METALLIC ELEMENTS</topic><topic>PERFORMING OPERATIONS</topic><topic>PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL</topic><topic>THEIR RELEVANT APPARATUS</topic><topic>TRANSPORTING</topic><toplevel>online_resources</toplevel><creatorcontrib>MERRIAM JAY S</creatorcontrib><creatorcontrib>HOGG CECIL B</creatorcontrib><collection>esp@cenet</collection></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext_linktorsrc</fulltext></delivery><addata><au>MERRIAM JAY S</au><au>HOGG CECIL B</au><format>patent</format><genre>patent</genre><ristype>GEN</ristype><title>CATALYST FOR CORBON MONOXIDE CONVERSION IN SOUR GAS</title><date>1987-09-26</date><risdate>1987</risdate><abstract>A sulphactive CO conversion catalyst comprises(a) an aluminous catalyst carrier; (b) a catalytically active metal compd. from Co or Ni oxide or sulphide or an oxide or sulphide of Gp.(V), (VI), or (VII) transition element; (c) a promotional amt. alkali metal compd., pref. K2CO3; and (d) a promotional amt. oxide or sulphide of fourth period metal at number 22-25 inclusive, pref. Mn as less than 5 wt.%, expressed as the oxide. CO is catalytically converted with steam to form H2 and CO2, by passing a synthesis gas mixt. of CO and steam, over the catalyst, at 150-540 deg.C but above the dew point of the sybthesis gas mixt.; and at pressure below the dew point pressure of the gas mixt.</abstract><edition>4</edition><oa>free_for_read</oa></addata></record> |
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| subjects | CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOIDCHEMISTRY CHEMISTRY COMPOUNDS THEREOF INORGANIC CHEMISTRY METALLURGY NON-METALLIC ELEMENTS PERFORMING OPERATIONS PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL THEIR RELEVANT APPARATUS TRANSPORTING |
| title | CATALYST FOR CORBON MONOXIDE CONVERSION IN SOUR GAS |
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