VERFAHREN UND ANLAGE ZUR HERSTELLUNG VON METHANOL
In the production of methanol from a synthesis gas containing hydrogen and carbon oxides, the synthesis gas is passed through a first, preferably water-cooled reactor, in which a part of the carbon oxides is catalytically converted to methanol. The obtained mixture containing synthesis gas and metha...
Gespeichert in:
Hauptverfasser: | , |
---|---|
Format: | Patent |
Sprache: | ger |
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 | BORMANN, ANDREAS MUELLER, DIERK |
description | In the production of methanol from a synthesis gas containing hydrogen and carbon oxides, the synthesis gas is passed through a first, preferably water-cooled reactor, in which a part of the carbon oxides is catalytically converted to methanol. The obtained mixture containing synthesis gas and methanol vapor is supplied to a second, preferably gas-cooled reactor, in which a further part of the carbon oxides is converted to methanol. Subsequently, methanol is separated from the synthesis gas, and the synthesis gas is recirculated to the first reactor. To achieve a maximum methanol yield even with an aged catalyst, a partial stream of the synthesis gas is guided past the first reactor and introduced directly into the second reactor. |
format | Patent |
fullrecord | <record><control><sourceid>epo_EVB</sourceid><recordid>TN_cdi_epo_espacenet_ATE528274TT1</recordid><sourceformat>XML</sourceformat><sourcesystem>PC</sourcesystem><sourcerecordid>ATE528274TT1</sourcerecordid><originalsourceid>FETCH-epo_espacenet_ATE528274TT13</originalsourceid><addsrcrecordid>eNrjZDAMcw1yc_QIcvVTCPVzUXD083F0d1WICg1S8HANCg5x9fEJ9XNXCPP3U_B1DfFw9PP34WFgTUvMKU7lhdLcDIpuriHOHrqpBfnxqcUFicmpeakl8Y4hrqZGFkbmJiEhhsbEqAEAaYAnOw</addsrcrecordid><sourcetype>Open Access Repository</sourcetype><iscdi>true</iscdi><recordtype>patent</recordtype></control><display><type>patent</type><title>VERFAHREN UND ANLAGE ZUR HERSTELLUNG VON METHANOL</title><source>esp@cenet</source><creator>BORMANN, ANDREAS ; MUELLER, DIERK</creator><creatorcontrib>BORMANN, ANDREAS ; MUELLER, DIERK</creatorcontrib><description>In the production of methanol from a synthesis gas containing hydrogen and carbon oxides, the synthesis gas is passed through a first, preferably water-cooled reactor, in which a part of the carbon oxides is catalytically converted to methanol. The obtained mixture containing synthesis gas and methanol vapor is supplied to a second, preferably gas-cooled reactor, in which a further part of the carbon oxides is converted to methanol. Subsequently, methanol is separated from the synthesis gas, and the synthesis gas is recirculated to the first reactor. To achieve a maximum methanol yield even with an aged catalyst, a partial stream of the synthesis gas is guided past the first reactor and introduced directly into the second reactor.</description><language>ger</language><creationdate>2011</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=20111015&DB=EPODOC&CC=AT&NR=E528274T1$$EHTML$$P50$$Gepo$$Hfree_for_read</linktohtml><link.rule.ids>230,309,781,886,25569,76552</link.rule.ids><linktorsrc>$$Uhttps://worldwide.espacenet.com/publicationDetails/biblio?FT=D&date=20111015&DB=EPODOC&CC=AT&NR=E528274T1$$EView_record_in_European_Patent_Office$$FView_record_in_$$GEuropean_Patent_Office$$Hfree_for_read</linktorsrc></links><search><creatorcontrib>BORMANN, ANDREAS</creatorcontrib><creatorcontrib>MUELLER, DIERK</creatorcontrib><title>VERFAHREN UND ANLAGE ZUR HERSTELLUNG VON METHANOL</title><description>In the production of methanol from a synthesis gas containing hydrogen and carbon oxides, the synthesis gas is passed through a first, preferably water-cooled reactor, in which a part of the carbon oxides is catalytically converted to methanol. The obtained mixture containing synthesis gas and methanol vapor is supplied to a second, preferably gas-cooled reactor, in which a further part of the carbon oxides is converted to methanol. Subsequently, methanol is separated from the synthesis gas, and the synthesis gas is recirculated to the first reactor. To achieve a maximum methanol yield even with an aged catalyst, a partial stream of the synthesis gas is guided past the first reactor and introduced directly into the second reactor.</description><fulltext>true</fulltext><rsrctype>patent</rsrctype><creationdate>2011</creationdate><recordtype>patent</recordtype><sourceid>EVB</sourceid><recordid>eNrjZDAMcw1yc_QIcvVTCPVzUXD083F0d1WICg1S8HANCg5x9fEJ9XNXCPP3U_B1DfFw9PP34WFgTUvMKU7lhdLcDIpuriHOHrqpBfnxqcUFicmpeakl8Y4hrqZGFkbmJiEhhsbEqAEAaYAnOw</recordid><startdate>20111015</startdate><enddate>20111015</enddate><creator>BORMANN, ANDREAS</creator><creator>MUELLER, DIERK</creator><scope>EVB</scope></search><sort><creationdate>20111015</creationdate><title>VERFAHREN UND ANLAGE ZUR HERSTELLUNG VON METHANOL</title><author>BORMANN, ANDREAS ; MUELLER, DIERK</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-epo_espacenet_ATE528274TT13</frbrgroupid><rsrctype>patents</rsrctype><prefilter>patents</prefilter><language>ger</language><creationdate>2011</creationdate><toplevel>online_resources</toplevel><creatorcontrib>BORMANN, ANDREAS</creatorcontrib><creatorcontrib>MUELLER, DIERK</creatorcontrib><collection>esp@cenet</collection></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext_linktorsrc</fulltext></delivery><addata><au>BORMANN, ANDREAS</au><au>MUELLER, DIERK</au><format>patent</format><genre>patent</genre><ristype>GEN</ristype><title>VERFAHREN UND ANLAGE ZUR HERSTELLUNG VON METHANOL</title><date>2011-10-15</date><risdate>2011</risdate><abstract>In the production of methanol from a synthesis gas containing hydrogen and carbon oxides, the synthesis gas is passed through a first, preferably water-cooled reactor, in which a part of the carbon oxides is catalytically converted to methanol. The obtained mixture containing synthesis gas and methanol vapor is supplied to a second, preferably gas-cooled reactor, in which a further part of the carbon oxides is converted to methanol. Subsequently, methanol is separated from the synthesis gas, and the synthesis gas is recirculated to the first reactor. To achieve a maximum methanol yield even with an aged catalyst, a partial stream of the synthesis gas is guided past the first reactor and introduced directly into the second reactor.</abstract><oa>free_for_read</oa></addata></record> |
fulltext | fulltext_linktorsrc |
identifier | |
ispartof | |
issn | |
language | ger |
recordid | cdi_epo_espacenet_ATE528274TT1 |
source | esp@cenet |
title | VERFAHREN UND ANLAGE ZUR HERSTELLUNG VON METHANOL |
url | https://sfx.bib-bvb.de/sfx_tum?ctx_ver=Z39.88-2004&ctx_enc=info:ofi/enc:UTF-8&ctx_tim=2024-12-15T23%3A00%3A22IST&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=BORMANN,%20ANDREAS&rft.date=2011-10-15&rft_id=info:doi/&rft_dat=%3Cepo_EVB%3EATE528274TT1%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 |