TEMPERATURE CONTROLLED IN SITU WAX PURIFICATION
A HYDROCARBON WAX PRODUCT FROM A HCS SLURRY COMPRISING LIQUID SYNTHESIS PRODUCT AND CATALYST PARTICLES IS PURIFIED BY CIRCULATING THE SLURRY (18) FROM A SYNTHESIS ZONE (52) WITH A FIRST TEMPERATURE THROUGH A TREATMENT ZONE (38) WITH A SECOND TEMPERATURE IN WHICH A HYDROGEN-CONTAINING TREATMENT GAS C...
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 | LOUIS FRANCIS BURNS GEOFFREY RHYS SAY GREGG JOHNSTON HOWSMON CHARLES HARRISON MAULDIN ROBERT JAY WITTENBRINK |
| description | A HYDROCARBON WAX PRODUCT FROM A HCS SLURRY COMPRISING LIQUID SYNTHESIS PRODUCT AND CATALYST PARTICLES IS PURIFIED BY CIRCULATING THE SLURRY (18) FROM A SYNTHESIS ZONE (52) WITH A FIRST TEMPERATURE THROUGH A TREATMENT ZONE (38) WITH A SECOND TEMPERATURE IN WHICH A HYDROGEN-CONTAINING TREATMENT GAS CONTACTS THE SLURRY (18). THE GAS TREATMENT REMOVES IMPURITIES FROM THE HYDROCARBON WAX PRODUCT AND ALSO REMOVES CATALYST DE-ACTIVATING SPECIES WHICH MAY BE PRESENT IN THE SLURRY (18). PURIFIED WAX PRODUCT IS SEPARATED AND REMOVED FROM THE TREATED SLURRY (49) VIA WAX WITHDRAWAL MEANS (66). THIS AVOIDS OR MINIMIZES THE NEED FOR FURTHER TREATING THE WAX PRODUCT. REMAINING TREATED SLURRY (49) MAY BE RETURNED TO THE SYNTHESIS ZONE (52). FIG. 1 |
| format | Patent |
| fullrecord | <record><control><sourceid>epo_EVB</sourceid><recordid>TN_cdi_epo_espacenet_MY122884A</recordid><sourceformat>XML</sourceformat><sourcesystem>PC</sourcesystem><sourcerecordid>MY122884A</sourcerecordid><originalsourceid>FETCH-epo_espacenet_MY122884A3</originalsourceid><addsrcrecordid>eNrjZNAPcfUNcA1yDAkNclVw9vcLCfL38XF1UfD0Uwj2DAlVCHeMUAgIDfJ083R2DPH09-NhYE1LzClO5YXS3Axybq4hzh66qQX58anFBYnJqXmpJfG-kYZGRhYWJo7GBBUAAFhaJUk</addsrcrecordid><sourcetype>Open Access Repository</sourcetype><iscdi>true</iscdi><recordtype>patent</recordtype></control><display><type>patent</type><title>TEMPERATURE CONTROLLED IN SITU WAX PURIFICATION</title><source>esp@cenet</source><creator>LOUIS FRANCIS BURNS ; GEOFFREY RHYS SAY ; GREGG JOHNSTON HOWSMON ; CHARLES HARRISON MAULDIN ; ROBERT JAY WITTENBRINK</creator><creatorcontrib>LOUIS FRANCIS BURNS ; GEOFFREY RHYS SAY ; GREGG JOHNSTON HOWSMON ; CHARLES HARRISON MAULDIN ; ROBERT JAY WITTENBRINK</creatorcontrib><description>A HYDROCARBON WAX PRODUCT FROM A HCS SLURRY COMPRISING LIQUID SYNTHESIS PRODUCT AND CATALYST PARTICLES IS PURIFIED BY CIRCULATING THE SLURRY (18) FROM A SYNTHESIS ZONE (52) WITH A FIRST TEMPERATURE THROUGH A TREATMENT ZONE (38) WITH A SECOND TEMPERATURE IN WHICH A HYDROGEN-CONTAINING TREATMENT GAS CONTACTS THE SLURRY (18). THE GAS TREATMENT REMOVES IMPURITIES FROM THE HYDROCARBON WAX PRODUCT AND ALSO REMOVES CATALYST DE-ACTIVATING SPECIES WHICH MAY BE PRESENT IN THE SLURRY (18). PURIFIED WAX PRODUCT IS SEPARATED AND REMOVED FROM THE TREATED SLURRY (49) VIA WAX WITHDRAWAL MEANS (66). THIS AVOIDS OR MINIMIZES THE NEED FOR FURTHER TREATING THE WAX PRODUCT. REMAINING TREATED SLURRY (49) MAY BE RETURNED TO THE SYNTHESIS ZONE (52). FIG. 1</description><language>eng</language><subject>ACYCLIC OR CARBOCYCLIC COMPOUNDS ; APPARATUS THEREFOR ; CHEMISTRY ; CRACKING HYDROCARBON OILS ; FUELS ; GENERAL METHODS OF ORGANIC CHEMISTRY ; LUBRICANTS ; METALLURGY ; MINERAL WAXES ; ORGANIC CHEMISTRY ; 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>2006</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=20060531&DB=EPODOC&CC=MY&NR=122884A$$EHTML$$P50$$Gepo$$Hfree_for_read</linktohtml><link.rule.ids>230,308,780,885,25564,76547</link.rule.ids><linktorsrc>$$Uhttps://worldwide.espacenet.com/publicationDetails/biblio?FT=D&date=20060531&DB=EPODOC&CC=MY&NR=122884A$$EView_record_in_European_Patent_Office$$FView_record_in_$$GEuropean_Patent_Office$$Hfree_for_read</linktorsrc></links><search><creatorcontrib>LOUIS FRANCIS BURNS</creatorcontrib><creatorcontrib>GEOFFREY RHYS SAY</creatorcontrib><creatorcontrib>GREGG JOHNSTON HOWSMON</creatorcontrib><creatorcontrib>CHARLES HARRISON MAULDIN</creatorcontrib><creatorcontrib>ROBERT JAY WITTENBRINK</creatorcontrib><title>TEMPERATURE CONTROLLED IN SITU WAX PURIFICATION</title><description>A HYDROCARBON WAX PRODUCT FROM A HCS SLURRY COMPRISING LIQUID SYNTHESIS PRODUCT AND CATALYST PARTICLES IS PURIFIED BY CIRCULATING THE SLURRY (18) FROM A SYNTHESIS ZONE (52) WITH A FIRST TEMPERATURE THROUGH A TREATMENT ZONE (38) WITH A SECOND TEMPERATURE IN WHICH A HYDROGEN-CONTAINING TREATMENT GAS CONTACTS THE SLURRY (18). THE GAS TREATMENT REMOVES IMPURITIES FROM THE HYDROCARBON WAX PRODUCT AND ALSO REMOVES CATALYST DE-ACTIVATING SPECIES WHICH MAY BE PRESENT IN THE SLURRY (18). PURIFIED WAX PRODUCT IS SEPARATED AND REMOVED FROM THE TREATED SLURRY (49) VIA WAX WITHDRAWAL MEANS (66). THIS AVOIDS OR MINIMIZES THE NEED FOR FURTHER TREATING THE WAX PRODUCT. REMAINING TREATED SLURRY (49) MAY BE RETURNED TO THE SYNTHESIS ZONE (52). FIG. 1</description><subject>ACYCLIC OR CARBOCYCLIC COMPOUNDS</subject><subject>APPARATUS THEREFOR</subject><subject>CHEMISTRY</subject><subject>CRACKING HYDROCARBON OILS</subject><subject>FUELS</subject><subject>GENERAL METHODS OF ORGANIC CHEMISTRY</subject><subject>LUBRICANTS</subject><subject>METALLURGY</subject><subject>MINERAL WAXES</subject><subject>ORGANIC CHEMISTRY</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>2006</creationdate><recordtype>patent</recordtype><sourceid>EVB</sourceid><recordid>eNrjZNAPcfUNcA1yDAkNclVw9vcLCfL38XF1UfD0Uwj2DAlVCHeMUAgIDfJ083R2DPH09-NhYE1LzClO5YXS3Axybq4hzh66qQX58anFBYnJqXmpJfG-kYZGRhYWJo7GBBUAAFhaJUk</recordid><startdate>20060531</startdate><enddate>20060531</enddate><creator>LOUIS FRANCIS BURNS</creator><creator>GEOFFREY RHYS SAY</creator><creator>GREGG JOHNSTON HOWSMON</creator><creator>CHARLES HARRISON MAULDIN</creator><creator>ROBERT JAY WITTENBRINK</creator><scope>EVB</scope></search><sort><creationdate>20060531</creationdate><title>TEMPERATURE CONTROLLED IN SITU WAX PURIFICATION</title><author>LOUIS FRANCIS BURNS ; GEOFFREY RHYS SAY ; GREGG JOHNSTON HOWSMON ; CHARLES HARRISON MAULDIN ; ROBERT JAY WITTENBRINK</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-epo_espacenet_MY122884A3</frbrgroupid><rsrctype>patents</rsrctype><prefilter>patents</prefilter><language>eng</language><creationdate>2006</creationdate><topic>ACYCLIC OR CARBOCYCLIC COMPOUNDS</topic><topic>APPARATUS THEREFOR</topic><topic>CHEMISTRY</topic><topic>CRACKING HYDROCARBON OILS</topic><topic>FUELS</topic><topic>GENERAL METHODS OF ORGANIC CHEMISTRY</topic><topic>LUBRICANTS</topic><topic>METALLURGY</topic><topic>MINERAL WAXES</topic><topic>ORGANIC CHEMISTRY</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>LOUIS FRANCIS BURNS</creatorcontrib><creatorcontrib>GEOFFREY RHYS SAY</creatorcontrib><creatorcontrib>GREGG JOHNSTON HOWSMON</creatorcontrib><creatorcontrib>CHARLES HARRISON MAULDIN</creatorcontrib><creatorcontrib>ROBERT JAY WITTENBRINK</creatorcontrib><collection>esp@cenet</collection></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext_linktorsrc</fulltext></delivery><addata><au>LOUIS FRANCIS BURNS</au><au>GEOFFREY RHYS SAY</au><au>GREGG JOHNSTON HOWSMON</au><au>CHARLES HARRISON MAULDIN</au><au>ROBERT JAY WITTENBRINK</au><format>patent</format><genre>patent</genre><ristype>GEN</ristype><title>TEMPERATURE CONTROLLED IN SITU WAX PURIFICATION</title><date>2006-05-31</date><risdate>2006</risdate><abstract>A HYDROCARBON WAX PRODUCT FROM A HCS SLURRY COMPRISING LIQUID SYNTHESIS PRODUCT AND CATALYST PARTICLES IS PURIFIED BY CIRCULATING THE SLURRY (18) FROM A SYNTHESIS ZONE (52) WITH A FIRST TEMPERATURE THROUGH A TREATMENT ZONE (38) WITH A SECOND TEMPERATURE IN WHICH A HYDROGEN-CONTAINING TREATMENT GAS CONTACTS THE SLURRY (18). THE GAS TREATMENT REMOVES IMPURITIES FROM THE HYDROCARBON WAX PRODUCT AND ALSO REMOVES CATALYST DE-ACTIVATING SPECIES WHICH MAY BE PRESENT IN THE SLURRY (18). PURIFIED WAX PRODUCT IS SEPARATED AND REMOVED FROM THE TREATED SLURRY (49) VIA WAX WITHDRAWAL MEANS (66). THIS AVOIDS OR MINIMIZES THE NEED FOR FURTHER TREATING THE WAX PRODUCT. REMAINING TREATED SLURRY (49) MAY BE RETURNED TO THE SYNTHESIS ZONE (52). FIG. 1</abstract><oa>free_for_read</oa></addata></record> |
| fulltext | fulltext_linktorsrc |
| identifier | |
| ispartof | |
| issn | |
| language | eng |
| recordid | cdi_epo_espacenet_MY122884A |
| source | esp@cenet |
| subjects | ACYCLIC OR CARBOCYCLIC COMPOUNDS APPARATUS THEREFOR CHEMISTRY CRACKING HYDROCARBON OILS FUELS GENERAL METHODS OF ORGANIC CHEMISTRY LUBRICANTS METALLURGY MINERAL WAXES ORGANIC CHEMISTRY 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 | TEMPERATURE CONTROLLED IN SITU WAX PURIFICATION |
| url | https://sfx.bib-bvb.de/sfx_tum?ctx_ver=Z39.88-2004&ctx_enc=info:ofi/enc:UTF-8&ctx_tim=2025-01-03T20%3A49%3A31IST&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=LOUIS%20FRANCIS%20BURNS&rft.date=2006-05-31&rft_id=info:doi/&rft_dat=%3Cepo_EVB%3EMY122884A%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 |