PROCESS FOR THE PRODUCTION OF ETHANOL BY HYDROGENATION OF VAPORIZED ACETIC ACID

Vaporizing acetic acid in the presence of hydrogen to provide a vapor feed stream for a hydrogenation process that produces ethanol. The vaporizer forms a vapor feed stream and a blowdown stream having a weight ratio of the vapor feed stream to the blowdown stream of at least 2:1. The acetic acid ma...

Ausführliche Beschreibung

Gespeichert in:
Bibliographische Detailangaben
Hauptverfasser: GRUSENDORF, GERALD, WARNER, R. JAY, AMLEH, WAEL, JEVTIC, RADMILA, WEINER, HEIKO, HORTON, TRINITY, JOHNSTON, VICTOR J
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 GRUSENDORF, GERALD
WARNER, R. JAY
AMLEH, WAEL
JEVTIC, RADMILA
WEINER, HEIKO
HORTON, TRINITY
JOHNSTON, VICTOR J
description Vaporizing acetic acid in the presence of hydrogen to provide a vapor feed stream for a hydrogenation process that produces ethanol. The vaporizer forms a vapor feed stream and a blowdown stream having a weight ratio of the vapor feed stream to the blowdown stream of at least 2:1. The acetic acid may vaporized at a temperature below acetic acid's boiling point at the operating pressure of the reactor. The hydrogenation process produces a crude ethanol product and ethanol is separated from the crude product. In addition, at least one recycle stream comprising acetic acid and less than 1.0 wt. % compounds having a boiling point higher than acetic acid, may also be separated. The recycle streams may be introduced to the vaporizer along with acetic acid to form the vapor feed stream.
format Patent
fullrecord <record><control><sourceid>epo_EVB</sourceid><recordid>TN_cdi_epo_espacenet_SG182692A1</recordid><sourceformat>XML</sourceformat><sourcesystem>PC</sourcesystem><sourcerecordid>SG182692A1</sourcerecordid><originalsourceid>FETCH-epo_espacenet_SG182692A13</originalsourceid><addsrcrecordid>eNrjZPAPCPJ3dg0OVnDzD1II8XBVAPJdQp1DPP39FPzdFFxDPBz9_H0UnCIVPCJdgvzdXf0cYXJhjgH-QZ5Rri4Kjs6uIZ7OQMrThYeBNS0xpziVF0pzM8i7uYY4e-imFuTHpxYXJCan5qWWxAe7G1oYmVkaORoaE1YBAIlFLeU</addsrcrecordid><sourcetype>Open Access Repository</sourcetype><iscdi>true</iscdi><recordtype>patent</recordtype></control><display><type>patent</type><title>PROCESS FOR THE PRODUCTION OF ETHANOL BY HYDROGENATION OF VAPORIZED ACETIC ACID</title><source>esp@cenet</source><creator>GRUSENDORF, GERALD ; WARNER, R. JAY ; AMLEH, WAEL ; JEVTIC, RADMILA ; WEINER, HEIKO ; HORTON, TRINITY ; JOHNSTON, VICTOR J</creator><creatorcontrib>GRUSENDORF, GERALD ; WARNER, R. JAY ; AMLEH, WAEL ; JEVTIC, RADMILA ; WEINER, HEIKO ; HORTON, TRINITY ; JOHNSTON, VICTOR J</creatorcontrib><description>Vaporizing acetic acid in the presence of hydrogen to provide a vapor feed stream for a hydrogenation process that produces ethanol. The vaporizer forms a vapor feed stream and a blowdown stream having a weight ratio of the vapor feed stream to the blowdown stream of at least 2:1. The acetic acid may vaporized at a temperature below acetic acid's boiling point at the operating pressure of the reactor. The hydrogenation process produces a crude ethanol product and ethanol is separated from the crude product. In addition, at least one recycle stream comprising acetic acid and less than 1.0 wt. % compounds having a boiling point higher than acetic acid, may also be separated. The recycle streams may be introduced to the vaporizer along with acetic acid to form the vapor feed stream.</description><language>eng</language><subject>ACYCLIC OR CARBOCYCLIC COMPOUNDS ; CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOIDCHEMISTRY ; CHEMISTRY ; METALLURGY ; ORGANIC CHEMISTRY ; PERFORMING OPERATIONS ; PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL ; SEPARATION ; THEIR RELEVANT APPARATUS ; TRANSPORTING</subject><creationdate>2012</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&amp;date=20120830&amp;DB=EPODOC&amp;CC=SG&amp;NR=182692A1$$EHTML$$P50$$Gepo$$Hfree_for_read</linktohtml><link.rule.ids>230,308,776,881,25543,76293</link.rule.ids><linktorsrc>$$Uhttps://worldwide.espacenet.com/publicationDetails/biblio?FT=D&amp;date=20120830&amp;DB=EPODOC&amp;CC=SG&amp;NR=182692A1$$EView_record_in_European_Patent_Office$$FView_record_in_$$GEuropean_Patent_Office$$Hfree_for_read</linktorsrc></links><search><creatorcontrib>GRUSENDORF, GERALD</creatorcontrib><creatorcontrib>WARNER, R. JAY</creatorcontrib><creatorcontrib>AMLEH, WAEL</creatorcontrib><creatorcontrib>JEVTIC, RADMILA</creatorcontrib><creatorcontrib>WEINER, HEIKO</creatorcontrib><creatorcontrib>HORTON, TRINITY</creatorcontrib><creatorcontrib>JOHNSTON, VICTOR J</creatorcontrib><title>PROCESS FOR THE PRODUCTION OF ETHANOL BY HYDROGENATION OF VAPORIZED ACETIC ACID</title><description>Vaporizing acetic acid in the presence of hydrogen to provide a vapor feed stream for a hydrogenation process that produces ethanol. The vaporizer forms a vapor feed stream and a blowdown stream having a weight ratio of the vapor feed stream to the blowdown stream of at least 2:1. The acetic acid may vaporized at a temperature below acetic acid's boiling point at the operating pressure of the reactor. The hydrogenation process produces a crude ethanol product and ethanol is separated from the crude product. In addition, at least one recycle stream comprising acetic acid and less than 1.0 wt. % compounds having a boiling point higher than acetic acid, may also be separated. The recycle streams may be introduced to the vaporizer along with acetic acid to form the vapor feed stream.</description><subject>ACYCLIC OR CARBOCYCLIC COMPOUNDS</subject><subject>CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOIDCHEMISTRY</subject><subject>CHEMISTRY</subject><subject>METALLURGY</subject><subject>ORGANIC CHEMISTRY</subject><subject>PERFORMING OPERATIONS</subject><subject>PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL</subject><subject>SEPARATION</subject><subject>THEIR RELEVANT APPARATUS</subject><subject>TRANSPORTING</subject><fulltext>true</fulltext><rsrctype>patent</rsrctype><creationdate>2012</creationdate><recordtype>patent</recordtype><sourceid>EVB</sourceid><recordid>eNrjZPAPCPJ3dg0OVnDzD1II8XBVAPJdQp1DPP39FPzdFFxDPBz9_H0UnCIVPCJdgvzdXf0cYXJhjgH-QZ5Rri4Kjs6uIZ7OQMrThYeBNS0xpziVF0pzM8i7uYY4e-imFuTHpxYXJCan5qWWxAe7G1oYmVkaORoaE1YBAIlFLeU</recordid><startdate>20120830</startdate><enddate>20120830</enddate><creator>GRUSENDORF, GERALD</creator><creator>WARNER, R. JAY</creator><creator>AMLEH, WAEL</creator><creator>JEVTIC, RADMILA</creator><creator>WEINER, HEIKO</creator><creator>HORTON, TRINITY</creator><creator>JOHNSTON, VICTOR J</creator><scope>EVB</scope></search><sort><creationdate>20120830</creationdate><title>PROCESS FOR THE PRODUCTION OF ETHANOL BY HYDROGENATION OF VAPORIZED ACETIC ACID</title><author>GRUSENDORF, GERALD ; WARNER, R. JAY ; AMLEH, WAEL ; JEVTIC, RADMILA ; WEINER, HEIKO ; HORTON, TRINITY ; JOHNSTON, VICTOR J</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-epo_espacenet_SG182692A13</frbrgroupid><rsrctype>patents</rsrctype><prefilter>patents</prefilter><language>eng</language><creationdate>2012</creationdate><topic>ACYCLIC OR CARBOCYCLIC COMPOUNDS</topic><topic>CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOIDCHEMISTRY</topic><topic>CHEMISTRY</topic><topic>METALLURGY</topic><topic>ORGANIC CHEMISTRY</topic><topic>PERFORMING OPERATIONS</topic><topic>PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL</topic><topic>SEPARATION</topic><topic>THEIR RELEVANT APPARATUS</topic><topic>TRANSPORTING</topic><toplevel>online_resources</toplevel><creatorcontrib>GRUSENDORF, GERALD</creatorcontrib><creatorcontrib>WARNER, R. JAY</creatorcontrib><creatorcontrib>AMLEH, WAEL</creatorcontrib><creatorcontrib>JEVTIC, RADMILA</creatorcontrib><creatorcontrib>WEINER, HEIKO</creatorcontrib><creatorcontrib>HORTON, TRINITY</creatorcontrib><creatorcontrib>JOHNSTON, VICTOR J</creatorcontrib><collection>esp@cenet</collection></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext_linktorsrc</fulltext></delivery><addata><au>GRUSENDORF, GERALD</au><au>WARNER, R. JAY</au><au>AMLEH, WAEL</au><au>JEVTIC, RADMILA</au><au>WEINER, HEIKO</au><au>HORTON, TRINITY</au><au>JOHNSTON, VICTOR J</au><format>patent</format><genre>patent</genre><ristype>GEN</ristype><title>PROCESS FOR THE PRODUCTION OF ETHANOL BY HYDROGENATION OF VAPORIZED ACETIC ACID</title><date>2012-08-30</date><risdate>2012</risdate><abstract>Vaporizing acetic acid in the presence of hydrogen to provide a vapor feed stream for a hydrogenation process that produces ethanol. The vaporizer forms a vapor feed stream and a blowdown stream having a weight ratio of the vapor feed stream to the blowdown stream of at least 2:1. The acetic acid may vaporized at a temperature below acetic acid's boiling point at the operating pressure of the reactor. The hydrogenation process produces a crude ethanol product and ethanol is separated from the crude product. In addition, at least one recycle stream comprising acetic acid and less than 1.0 wt. % compounds having a boiling point higher than acetic acid, may also be separated. The recycle streams may be introduced to the vaporizer along with acetic acid to form the vapor feed stream.</abstract><oa>free_for_read</oa></addata></record>
fulltext fulltext_linktorsrc
identifier
ispartof
issn
language eng
recordid cdi_epo_espacenet_SG182692A1
source esp@cenet
subjects ACYCLIC OR CARBOCYCLIC COMPOUNDS
CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOIDCHEMISTRY
CHEMISTRY
METALLURGY
ORGANIC CHEMISTRY
PERFORMING OPERATIONS
PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
SEPARATION
THEIR RELEVANT APPARATUS
TRANSPORTING
title PROCESS FOR THE PRODUCTION OF ETHANOL BY HYDROGENATION OF VAPORIZED ACETIC ACID
url https://sfx.bib-bvb.de/sfx_tum?ctx_ver=Z39.88-2004&ctx_enc=info:ofi/enc:UTF-8&ctx_tim=2025-01-27T02%3A57%3A10IST&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=GRUSENDORF,%20GERALD&rft.date=2012-08-30&rft_id=info:doi/&rft_dat=%3Cepo_EVB%3ESG182692A1%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