Fractionation and desulphurisation of crude oil - in combined process without intermediate condnsn of vapour phase

Crude oil is processed by (A) heating to 360-380 degrees C under 20-70 atmos. after addn. of 20-500 Nm3 hydrogen per tonne, (B) separating the product into vapour and liquid phases, (C) treating the vapour phase without condnsn. or pressure increase by catalytic desulphurisation, with or without fur...

Ausführliche Beschreibung

Gespeichert in:
Bibliographische Detailangaben
Hauptverfasser: HUEWELS, WILHELM, SCHWALL, FRITZ, DOSTAL, PAUL
Format: Patent
Sprache:eng ; ger
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 HUEWELS, WILHELM
SCHWALL, FRITZ
DOSTAL, PAUL
description Crude oil is processed by (A) heating to 360-380 degrees C under 20-70 atmos. after addn. of 20-500 Nm3 hydrogen per tonne, (B) separating the product into vapour and liquid phases, (C) treating the vapour phase without condnsn. or pressure increase by catalytic desulphurisation, with or without further addn. of hydrogen, and (D) separating and recycling the unreacted hydrogen from the product. Costs of intermediate condensn., storage re-heating and re-compression of the vapour phase are eliminated.
format Patent
fullrecord <record><control><sourceid>epo_EVB</sourceid><recordid>TN_cdi_epo_espacenet_DE2359958A1</recordid><sourceformat>XML</sourceformat><sourcesystem>PC</sourcesystem><sourcerecordid>DE2359958A1</sourcerecordid><originalsourceid>FETCH-epo_espacenet_DE2359958A13</originalsourceid><addsrcrecordid>eNqNizsOwkAMRNNQIOAOvkAKiCKREkEiDkAfmV1HsZTYq_UuXJ_wOQDNjDTvzbqIXUSXWAXfASgePFmewpgj23fUAVzMnkB5ghJYwOl8ZyEPIaojM3hyGjWnhSWKM3nGRIslXuzzf2DQHCGMaLQtVgNORrtfbwro2tv5WlLQniygI6HUX9pDVTdNfTztqz-UF6uQRCc</addsrcrecordid><sourcetype>Open Access Repository</sourcetype><iscdi>true</iscdi><recordtype>patent</recordtype></control><display><type>patent</type><title>Fractionation and desulphurisation of crude oil - in combined process without intermediate condnsn of vapour phase</title><source>esp@cenet</source><creator>HUEWELS, WILHELM ; SCHWALL, FRITZ ; DOSTAL, PAUL</creator><creatorcontrib>HUEWELS, WILHELM ; SCHWALL, FRITZ ; DOSTAL, PAUL</creatorcontrib><description>Crude oil is processed by (A) heating to 360-380 degrees C under 20-70 atmos. after addn. of 20-500 Nm3 hydrogen per tonne, (B) separating the product into vapour and liquid phases, (C) treating the vapour phase without condnsn. or pressure increase by catalytic desulphurisation, with or without further addn. of hydrogen, and (D) separating and recycling the unreacted hydrogen from the product. Costs of intermediate condensn., storage re-heating and re-compression of the vapour phase are eliminated.</description><edition>2</edition><language>eng ; ger</language><subject>CHEMISTRY ; CRACKING HYDROCARBON OILS ; FUELS ; LUBRICANTS ; METALLURGY ; MINERAL WAXES ; PEAT ; PETROLEUM, GAS OR COKE INDUSTRIES ; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVEHYDROGENATION, OLIGOMERISATION, POLYMERISATION ; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, ORGASES ; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS ; REFORMING OF NAPHTHA ; TECHNICAL GASES CONTAINING CARBON MONOXIDE</subject><creationdate>1975</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=19750612&amp;DB=EPODOC&amp;CC=DE&amp;NR=2359958A1$$EHTML$$P50$$Gepo$$Hfree_for_read</linktohtml><link.rule.ids>230,308,780,885,25564,76547</link.rule.ids><linktorsrc>$$Uhttps://worldwide.espacenet.com/publicationDetails/biblio?FT=D&amp;date=19750612&amp;DB=EPODOC&amp;CC=DE&amp;NR=2359958A1$$EView_record_in_European_Patent_Office$$FView_record_in_$$GEuropean_Patent_Office$$Hfree_for_read</linktorsrc></links><search><creatorcontrib>HUEWELS, WILHELM</creatorcontrib><creatorcontrib>SCHWALL, FRITZ</creatorcontrib><creatorcontrib>DOSTAL, PAUL</creatorcontrib><title>Fractionation and desulphurisation of crude oil - in combined process without intermediate condnsn of vapour phase</title><description>Crude oil is processed by (A) heating to 360-380 degrees C under 20-70 atmos. after addn. of 20-500 Nm3 hydrogen per tonne, (B) separating the product into vapour and liquid phases, (C) treating the vapour phase without condnsn. or pressure increase by catalytic desulphurisation, with or without further addn. of hydrogen, and (D) separating and recycling the unreacted hydrogen from the product. Costs of intermediate condensn., storage re-heating and re-compression of the vapour phase are eliminated.</description><subject>CHEMISTRY</subject><subject>CRACKING HYDROCARBON OILS</subject><subject>FUELS</subject><subject>LUBRICANTS</subject><subject>METALLURGY</subject><subject>MINERAL WAXES</subject><subject>PEAT</subject><subject>PETROLEUM, GAS OR COKE INDUSTRIES</subject><subject>PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVEHYDROGENATION, OLIGOMERISATION, POLYMERISATION</subject><subject>RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, ORGASES</subject><subject>REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS</subject><subject>REFORMING OF NAPHTHA</subject><subject>TECHNICAL GASES CONTAINING CARBON MONOXIDE</subject><fulltext>true</fulltext><rsrctype>patent</rsrctype><creationdate>1975</creationdate><recordtype>patent</recordtype><sourceid>EVB</sourceid><recordid>eNqNizsOwkAMRNNQIOAOvkAKiCKREkEiDkAfmV1HsZTYq_UuXJ_wOQDNjDTvzbqIXUSXWAXfASgePFmewpgj23fUAVzMnkB5ghJYwOl8ZyEPIaojM3hyGjWnhSWKM3nGRIslXuzzf2DQHCGMaLQtVgNORrtfbwro2tv5WlLQniygI6HUX9pDVTdNfTztqz-UF6uQRCc</recordid><startdate>19750612</startdate><enddate>19750612</enddate><creator>HUEWELS, WILHELM</creator><creator>SCHWALL, FRITZ</creator><creator>DOSTAL, PAUL</creator><scope>EVB</scope></search><sort><creationdate>19750612</creationdate><title>Fractionation and desulphurisation of crude oil - in combined process without intermediate condnsn of vapour phase</title><author>HUEWELS, WILHELM ; SCHWALL, FRITZ ; DOSTAL, PAUL</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-epo_espacenet_DE2359958A13</frbrgroupid><rsrctype>patents</rsrctype><prefilter>patents</prefilter><language>eng ; ger</language><creationdate>1975</creationdate><topic>CHEMISTRY</topic><topic>CRACKING HYDROCARBON OILS</topic><topic>FUELS</topic><topic>LUBRICANTS</topic><topic>METALLURGY</topic><topic>MINERAL WAXES</topic><topic>PEAT</topic><topic>PETROLEUM, GAS OR COKE INDUSTRIES</topic><topic>PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVEHYDROGENATION, OLIGOMERISATION, POLYMERISATION</topic><topic>RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, ORGASES</topic><topic>REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS</topic><topic>REFORMING OF NAPHTHA</topic><topic>TECHNICAL GASES CONTAINING CARBON MONOXIDE</topic><toplevel>online_resources</toplevel><creatorcontrib>HUEWELS, WILHELM</creatorcontrib><creatorcontrib>SCHWALL, FRITZ</creatorcontrib><creatorcontrib>DOSTAL, PAUL</creatorcontrib><collection>esp@cenet</collection></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext_linktorsrc</fulltext></delivery><addata><au>HUEWELS, WILHELM</au><au>SCHWALL, FRITZ</au><au>DOSTAL, PAUL</au><format>patent</format><genre>patent</genre><ristype>GEN</ristype><title>Fractionation and desulphurisation of crude oil - in combined process without intermediate condnsn of vapour phase</title><date>1975-06-12</date><risdate>1975</risdate><abstract>Crude oil is processed by (A) heating to 360-380 degrees C under 20-70 atmos. after addn. of 20-500 Nm3 hydrogen per tonne, (B) separating the product into vapour and liquid phases, (C) treating the vapour phase without condnsn. or pressure increase by catalytic desulphurisation, with or without further addn. of hydrogen, and (D) separating and recycling the unreacted hydrogen from the product. Costs of intermediate condensn., storage re-heating and re-compression of the vapour phase are eliminated.</abstract><edition>2</edition><oa>free_for_read</oa></addata></record>
fulltext fulltext_linktorsrc
identifier
ispartof
issn
language eng ; ger
recordid cdi_epo_espacenet_DE2359958A1
source esp@cenet
subjects CHEMISTRY
CRACKING HYDROCARBON OILS
FUELS
LUBRICANTS
METALLURGY
MINERAL WAXES
PEAT
PETROLEUM, GAS OR COKE INDUSTRIES
PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVEHYDROGENATION, OLIGOMERISATION, POLYMERISATION
RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, ORGASES
REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS
REFORMING OF NAPHTHA
TECHNICAL GASES CONTAINING CARBON MONOXIDE
title Fractionation and desulphurisation of crude oil - in combined process without intermediate condnsn of vapour phase
url https://sfx.bib-bvb.de/sfx_tum?ctx_ver=Z39.88-2004&ctx_enc=info:ofi/enc:UTF-8&ctx_tim=2024-12-29T05%3A49%3A09IST&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=HUEWELS,%20WILHELM&rft.date=1975-06-12&rft_id=info:doi/&rft_dat=%3Cepo_EVB%3EDE2359958A1%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