A METHOD OF PRODUCING A SYNTHESIS GAS RICH IN CARBON MONOXIDE
1,212,817. Making a carbon monoxide-rich gas. METALLGESELLSCHAFT A.G. 12 Aug., 1969 [13 Aug., 1968], No. 40246/69. Heading C5E. In a method of producing a CO-rich gas for oxo-synthesis by steam-cracking a liquid or normally gaseous hydrocarbon over a catalyst, CO 2 is scrubbed out of the cracked gas...
Gespeichert in:
| Hauptverfasser: | , , , , |
|---|---|
| Format: | Patent |
| Sprache: | eng |
| Schlagworte: | |
| Online-Zugang: | Volltext bestellen |
| Tags: |
Tag hinzufügen
Keine Tags, Fügen Sie den ersten Tag hinzu!
|
| container_end_page | |
|---|---|
| container_issue | |
| container_start_page | |
| container_title | |
| container_volume | |
| creator | HEINZ HILLER EMIL SUPP HEINZ JOCKEL JOSEF PESL MIRON BREJC |
| description | 1,212,817. Making a carbon monoxide-rich gas. METALLGESELLSCHAFT A.G. 12 Aug., 1969 [13 Aug., 1968], No. 40246/69. Heading C5E. In a method of producing a CO-rich gas for oxo-synthesis by steam-cracking a liquid or normally gaseous hydrocarbon over a catalyst, CO 2 is scrubbed out of the cracked gas and recycled to the cracking stage, and at least part of the CO 2 -free gas is separated into a CO and an H 2 fraction, the CO fraction being mixed either with the other part of the CO,-free gas mixture, cr with part of the H 2 fraction. Surplus H 2 is available for desulphurizing the feedstock. If the feedstock is a liquid, all the CO 2 - free gas may be subjected to the separating step, and the feedstock may be pre-cracked over a Ni/Mg silicate catalyst to produce a CH 4 - rich gas which is then cracked with the CO 2 over a Ni/alumina or Ni/aluminium silicate catalyst. The precracking is carried out at 400‹ to 550‹ C., and the main cracking at above 750‹ C. In one example the feedstock is natural gas. |
| format | Patent |
| fullrecord | <record><control><sourceid>epo_EVB</sourceid><recordid>TN_cdi_epo_espacenet_GB1212817A</recordid><sourceformat>XML</sourceformat><sourcesystem>PC</sourcesystem><sourcerecordid>GB1212817A</sourcerecordid><originalsourceid>FETCH-epo_espacenet_GB1212817A3</originalsourceid><addsrcrecordid>eNrjZLB1VPB1DfHwd1Hwd1MICPJ3CXX29HNXcFQIjvQL8XAN9gxWcHcMVgjydPZQ8PRTcHYMcvL3U_D19_OP8HRx5WFgTUvMKU7lhdLcDPJuriHOHrqpBfnxqcUFicmpeakl8e5OhkaGRhaG5o7GhFUAAFPJKHk</addsrcrecordid><sourcetype>Open Access Repository</sourcetype><iscdi>true</iscdi><recordtype>patent</recordtype></control><display><type>patent</type><title>A METHOD OF PRODUCING A SYNTHESIS GAS RICH IN CARBON MONOXIDE</title><source>esp@cenet</source><creator>HEINZ HILLER ; EMIL SUPP ; HEINZ JOCKEL ; JOSEF PESL ; MIRON BREJC</creator><creatorcontrib>HEINZ HILLER ; EMIL SUPP ; HEINZ JOCKEL ; JOSEF PESL ; MIRON BREJC</creatorcontrib><description>1,212,817. Making a carbon monoxide-rich gas. METALLGESELLSCHAFT A.G. 12 Aug., 1969 [13 Aug., 1968], No. 40246/69. Heading C5E. In a method of producing a CO-rich gas for oxo-synthesis by steam-cracking a liquid or normally gaseous hydrocarbon over a catalyst, CO 2 is scrubbed out of the cracked gas and recycled to the cracking stage, and at least part of the CO 2 -free gas is separated into a CO and an H 2 fraction, the CO fraction being mixed either with the other part of the CO,-free gas mixture, cr with part of the H 2 fraction. Surplus H 2 is available for desulphurizing the feedstock. If the feedstock is a liquid, all the CO 2 - free gas may be subjected to the separating step, and the feedstock may be pre-cracked over a Ni/Mg silicate catalyst to produce a CH 4 - rich gas which is then cracked with the CO 2 over a Ni/alumina or Ni/aluminium silicate catalyst. The precracking is carried out at 400‹ to 550‹ C., and the main cracking at above 750‹ C. In one example the feedstock is natural gas.</description><language>eng</language><subject>CHEMISTRY ; COMPOUNDS THEREOF ; INORGANIC CHEMISTRY ; METALLURGY ; NON-METALLIC ELEMENTS</subject><creationdate>1970</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=19701118&DB=EPODOC&CC=GB&NR=1212817A$$EHTML$$P50$$Gepo$$Hfree_for_read</linktohtml><link.rule.ids>230,308,780,885,25563,76418</link.rule.ids><linktorsrc>$$Uhttps://worldwide.espacenet.com/publicationDetails/biblio?FT=D&date=19701118&DB=EPODOC&CC=GB&NR=1212817A$$EView_record_in_European_Patent_Office$$FView_record_in_$$GEuropean_Patent_Office$$Hfree_for_read</linktorsrc></links><search><creatorcontrib>HEINZ HILLER</creatorcontrib><creatorcontrib>EMIL SUPP</creatorcontrib><creatorcontrib>HEINZ JOCKEL</creatorcontrib><creatorcontrib>JOSEF PESL</creatorcontrib><creatorcontrib>MIRON BREJC</creatorcontrib><title>A METHOD OF PRODUCING A SYNTHESIS GAS RICH IN CARBON MONOXIDE</title><description>1,212,817. Making a carbon monoxide-rich gas. METALLGESELLSCHAFT A.G. 12 Aug., 1969 [13 Aug., 1968], No. 40246/69. Heading C5E. In a method of producing a CO-rich gas for oxo-synthesis by steam-cracking a liquid or normally gaseous hydrocarbon over a catalyst, CO 2 is scrubbed out of the cracked gas and recycled to the cracking stage, and at least part of the CO 2 -free gas is separated into a CO and an H 2 fraction, the CO fraction being mixed either with the other part of the CO,-free gas mixture, cr with part of the H 2 fraction. Surplus H 2 is available for desulphurizing the feedstock. If the feedstock is a liquid, all the CO 2 - free gas may be subjected to the separating step, and the feedstock may be pre-cracked over a Ni/Mg silicate catalyst to produce a CH 4 - rich gas which is then cracked with the CO 2 over a Ni/alumina or Ni/aluminium silicate catalyst. The precracking is carried out at 400‹ to 550‹ C., and the main cracking at above 750‹ C. In one example the feedstock is natural gas.</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>1970</creationdate><recordtype>patent</recordtype><sourceid>EVB</sourceid><recordid>eNrjZLB1VPB1DfHwd1Hwd1MICPJ3CXX29HNXcFQIjvQL8XAN9gxWcHcMVgjydPZQ8PRTcHYMcvL3U_D19_OP8HRx5WFgTUvMKU7lhdLcDPJuriHOHrqpBfnxqcUFicmpeakl8e5OhkaGRhaG5o7GhFUAAFPJKHk</recordid><startdate>19701118</startdate><enddate>19701118</enddate><creator>HEINZ HILLER</creator><creator>EMIL SUPP</creator><creator>HEINZ JOCKEL</creator><creator>JOSEF PESL</creator><creator>MIRON BREJC</creator><scope>EVB</scope></search><sort><creationdate>19701118</creationdate><title>A METHOD OF PRODUCING A SYNTHESIS GAS RICH IN CARBON MONOXIDE</title><author>HEINZ HILLER ; EMIL SUPP ; HEINZ JOCKEL ; JOSEF PESL ; MIRON BREJC</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-epo_espacenet_GB1212817A3</frbrgroupid><rsrctype>patents</rsrctype><prefilter>patents</prefilter><language>eng</language><creationdate>1970</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>HEINZ HILLER</creatorcontrib><creatorcontrib>EMIL SUPP</creatorcontrib><creatorcontrib>HEINZ JOCKEL</creatorcontrib><creatorcontrib>JOSEF PESL</creatorcontrib><creatorcontrib>MIRON BREJC</creatorcontrib><collection>esp@cenet</collection></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext_linktorsrc</fulltext></delivery><addata><au>HEINZ HILLER</au><au>EMIL SUPP</au><au>HEINZ JOCKEL</au><au>JOSEF PESL</au><au>MIRON BREJC</au><format>patent</format><genre>patent</genre><ristype>GEN</ristype><title>A METHOD OF PRODUCING A SYNTHESIS GAS RICH IN CARBON MONOXIDE</title><date>1970-11-18</date><risdate>1970</risdate><abstract>1,212,817. Making a carbon monoxide-rich gas. METALLGESELLSCHAFT A.G. 12 Aug., 1969 [13 Aug., 1968], No. 40246/69. Heading C5E. In a method of producing a CO-rich gas for oxo-synthesis by steam-cracking a liquid or normally gaseous hydrocarbon over a catalyst, CO 2 is scrubbed out of the cracked gas and recycled to the cracking stage, and at least part of the CO 2 -free gas is separated into a CO and an H 2 fraction, the CO fraction being mixed either with the other part of the CO,-free gas mixture, cr with part of the H 2 fraction. Surplus H 2 is available for desulphurizing the feedstock. If the feedstock is a liquid, all the CO 2 - free gas may be subjected to the separating step, and the feedstock may be pre-cracked over a Ni/Mg silicate catalyst to produce a CH 4 - rich gas which is then cracked with the CO 2 over a Ni/alumina or Ni/aluminium silicate catalyst. The precracking is carried out at 400‹ to 550‹ C., and the main cracking at above 750‹ C. In one example the feedstock is natural gas.</abstract><oa>free_for_read</oa></addata></record> |
| fulltext | fulltext_linktorsrc |
| identifier | |
| ispartof | |
| issn | |
| language | eng |
| recordid | cdi_epo_espacenet_GB1212817A |
| source | esp@cenet |
| subjects | CHEMISTRY COMPOUNDS THEREOF INORGANIC CHEMISTRY METALLURGY NON-METALLIC ELEMENTS |
| title | A METHOD OF PRODUCING A SYNTHESIS GAS RICH IN CARBON MONOXIDE |
| url | https://sfx.bib-bvb.de/sfx_tum?ctx_ver=Z39.88-2004&ctx_enc=info:ofi/enc:UTF-8&ctx_tim=2025-01-08T15%3A42%3A25IST&url_ver=Z39.88-2004&url_ctx_fmt=infofi/fmt:kev:mtx:ctx&rfr_id=info:sid/primo.exlibrisgroup.com:primo3-Article-epo_EVB&rft_val_fmt=info:ofi/fmt:kev:mtx:patent&rft.genre=patent&rft.au=HEINZ%20HILLER&rft.date=1970-11-18&rft_id=info:doi/&rft_dat=%3Cepo_EVB%3EGB1212817A%3C/epo_EVB%3E%3Curl%3E%3C/url%3E&disable_directlink=true&sfx.directlink=off&sfx.report_link=0&rft_id=info:oai/&rft_id=info:pmid/&rfr_iscdi=true |