A DESULFURIZATION SYSTEM AND METHOD FOR DESULFURIZING A FUEL STREAM
A method for producing a substantially desulfurized hydrocarbon fuel stream at temperatures less than 100°C. The method includes providing a nondesulfurized fuel cell hydrocarbon fuel stream that may include water and passing the fuel stream through a zeolite Y adsorbent and a selective sulfur adsor...
Gespeichert in:
| Hauptverfasser: | , , , |
|---|---|
| Format: | Patent |
| Sprache: | eng ; fre |
| 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 | ANFANG, HANS-GEORG WAGNER, JON, P SPIVEY, R., STEVE RATNASAMY, CHANDRA |
| description | A method for producing a substantially desulfurized hydrocarbon fuel stream at temperatures less than 100°C. The method includes providing a nondesulfurized fuel cell hydrocarbon fuel stream that may include water and passing the fuel stream through a zeolite Y adsorbent and a selective sulfur adsorbent. The zeolite Y adsorbent may be exchanged with copper ions. The sequence of use depends on the particular sulfur compounds present in the fuel stream. The method produces a substantially desulfurized hydrocarbon fuel stream containing less than 50 ppb sulfur.
Le procédé ci-décrit permet de produire un flux de combustible hydrocarboné essentiellement désulfurisé à des températures inférieures à 100°C. Le procédé comprend l'utilisation d'un flux de combustible hydrocarboné pour pile à combustible non désulfurisé qui peut comprendre de l'eau et le passage du flux de combustible dans un adsorbant du type zéolite Y et dans un adsorbant sélectif de soufre. L'adsorbant de zéolite Y peut être soumis à un échange avec des ions cuivre. La séquence d'utilisation dépend des composés de soufre particuliers présents dans le flux de combustible. Le procédé donne un flux de combustible hydrocarboné essentiellement désulfurisé contenant moins de 50 ppb de soufre. |
| format | Patent |
| fullrecord | <record><control><sourceid>epo_EVB</sourceid><recordid>TN_cdi_epo_espacenet_WO2010141825A3</recordid><sourceformat>XML</sourceformat><sourcesystem>PC</sourcesystem><sourcerecordid>WO2010141825A3</sourcerecordid><originalsourceid>FETCH-epo_espacenet_WO2010141825A33</originalsourceid><addsrcrecordid>eNrjZHB2VHBxDQ71cQsN8oxyDPH091MIjgwOcfVVcPRzUfB1DfHwd1Fw8w9CUuXp567gqOAW6uqjEBwS5Oroy8PAmpaYU5zKC6W5GZTdXEOcPXRTC_LjU4sLEpNT81JL4sP9jQwMDQxNDC2MTB2NjYlTBQDsMix7</addsrcrecordid><sourcetype>Open Access Repository</sourcetype><iscdi>true</iscdi><recordtype>patent</recordtype></control><display><type>patent</type><title>A DESULFURIZATION SYSTEM AND METHOD FOR DESULFURIZING A FUEL STREAM</title><source>esp@cenet</source><creator>ANFANG, HANS-GEORG ; WAGNER, JON, P ; SPIVEY, R., STEVE ; RATNASAMY, CHANDRA</creator><creatorcontrib>ANFANG, HANS-GEORG ; WAGNER, JON, P ; SPIVEY, R., STEVE ; RATNASAMY, CHANDRA</creatorcontrib><description>A method for producing a substantially desulfurized hydrocarbon fuel stream at temperatures less than 100°C. The method includes providing a nondesulfurized fuel cell hydrocarbon fuel stream that may include water and passing the fuel stream through a zeolite Y adsorbent and a selective sulfur adsorbent. The zeolite Y adsorbent may be exchanged with copper ions. The sequence of use depends on the particular sulfur compounds present in the fuel stream. The method produces a substantially desulfurized hydrocarbon fuel stream containing less than 50 ppb sulfur.
Le procédé ci-décrit permet de produire un flux de combustible hydrocarboné essentiellement désulfurisé à des températures inférieures à 100°C. Le procédé comprend l'utilisation d'un flux de combustible hydrocarboné pour pile à combustible non désulfurisé qui peut comprendre de l'eau et le passage du flux de combustible dans un adsorbant du type zéolite Y et dans un adsorbant sélectif de soufre. L'adsorbant de zéolite Y peut être soumis à un échange avec des ions cuivre. La séquence d'utilisation dépend des composés de soufre particuliers présents dans le flux de combustible. Le procédé donne un flux de combustible hydrocarboné essentiellement désulfurisé contenant moins de 50 ppb de soufre.</description><language>eng ; fre</language><subject>CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOIDCHEMISTRY ; CHEMISTRY ; CRACKING HYDROCARBON OILS ; FUELS ; LUBRICANTS ; METALLURGY ; MINERAL WAXES ; PEAT ; PERFORMING OPERATIONS ; PETROLEUM, GAS OR COKE INDUSTRIES ; PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL ; 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 ; SEPARATION ; TECHNICAL GASES CONTAINING CARBON MONOXIDE ; THEIR RELEVANT APPARATUS ; TRANSPORTING</subject><creationdate>2013</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=20130425&DB=EPODOC&CC=WO&NR=2010141825A3$$EHTML$$P50$$Gepo$$Hfree_for_read</linktohtml><link.rule.ids>230,308,777,882,25545,76296</link.rule.ids><linktorsrc>$$Uhttps://worldwide.espacenet.com/publicationDetails/biblio?FT=D&date=20130425&DB=EPODOC&CC=WO&NR=2010141825A3$$EView_record_in_European_Patent_Office$$FView_record_in_$$GEuropean_Patent_Office$$Hfree_for_read</linktorsrc></links><search><creatorcontrib>ANFANG, HANS-GEORG</creatorcontrib><creatorcontrib>WAGNER, JON, P</creatorcontrib><creatorcontrib>SPIVEY, R., STEVE</creatorcontrib><creatorcontrib>RATNASAMY, CHANDRA</creatorcontrib><title>A DESULFURIZATION SYSTEM AND METHOD FOR DESULFURIZING A FUEL STREAM</title><description>A method for producing a substantially desulfurized hydrocarbon fuel stream at temperatures less than 100°C. The method includes providing a nondesulfurized fuel cell hydrocarbon fuel stream that may include water and passing the fuel stream through a zeolite Y adsorbent and a selective sulfur adsorbent. The zeolite Y adsorbent may be exchanged with copper ions. The sequence of use depends on the particular sulfur compounds present in the fuel stream. The method produces a substantially desulfurized hydrocarbon fuel stream containing less than 50 ppb sulfur.
Le procédé ci-décrit permet de produire un flux de combustible hydrocarboné essentiellement désulfurisé à des températures inférieures à 100°C. Le procédé comprend l'utilisation d'un flux de combustible hydrocarboné pour pile à combustible non désulfurisé qui peut comprendre de l'eau et le passage du flux de combustible dans un adsorbant du type zéolite Y et dans un adsorbant sélectif de soufre. L'adsorbant de zéolite Y peut être soumis à un échange avec des ions cuivre. La séquence d'utilisation dépend des composés de soufre particuliers présents dans le flux de combustible. Le procédé donne un flux de combustible hydrocarboné essentiellement désulfurisé contenant moins de 50 ppb de soufre.</description><subject>CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOIDCHEMISTRY</subject><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>PERFORMING OPERATIONS</subject><subject>PETROLEUM, GAS OR COKE INDUSTRIES</subject><subject>PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL</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>SEPARATION</subject><subject>TECHNICAL GASES CONTAINING CARBON MONOXIDE</subject><subject>THEIR RELEVANT APPARATUS</subject><subject>TRANSPORTING</subject><fulltext>true</fulltext><rsrctype>patent</rsrctype><creationdate>2013</creationdate><recordtype>patent</recordtype><sourceid>EVB</sourceid><recordid>eNrjZHB2VHBxDQ71cQsN8oxyDPH091MIjgwOcfVVcPRzUfB1DfHwd1Fw8w9CUuXp567gqOAW6uqjEBwS5Oroy8PAmpaYU5zKC6W5GZTdXEOcPXRTC_LjU4sLEpNT81JL4sP9jQwMDQxNDC2MTB2NjYlTBQDsMix7</recordid><startdate>20130425</startdate><enddate>20130425</enddate><creator>ANFANG, HANS-GEORG</creator><creator>WAGNER, JON, P</creator><creator>SPIVEY, R., STEVE</creator><creator>RATNASAMY, CHANDRA</creator><scope>EVB</scope></search><sort><creationdate>20130425</creationdate><title>A DESULFURIZATION SYSTEM AND METHOD FOR DESULFURIZING A FUEL STREAM</title><author>ANFANG, HANS-GEORG ; WAGNER, JON, P ; SPIVEY, R., STEVE ; RATNASAMY, CHANDRA</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-epo_espacenet_WO2010141825A33</frbrgroupid><rsrctype>patents</rsrctype><prefilter>patents</prefilter><language>eng ; fre</language><creationdate>2013</creationdate><topic>CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOIDCHEMISTRY</topic><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>PERFORMING OPERATIONS</topic><topic>PETROLEUM, GAS OR COKE INDUSTRIES</topic><topic>PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL</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>SEPARATION</topic><topic>TECHNICAL GASES CONTAINING CARBON MONOXIDE</topic><topic>THEIR RELEVANT APPARATUS</topic><topic>TRANSPORTING</topic><toplevel>online_resources</toplevel><creatorcontrib>ANFANG, HANS-GEORG</creatorcontrib><creatorcontrib>WAGNER, JON, P</creatorcontrib><creatorcontrib>SPIVEY, R., STEVE</creatorcontrib><creatorcontrib>RATNASAMY, CHANDRA</creatorcontrib><collection>esp@cenet</collection></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext_linktorsrc</fulltext></delivery><addata><au>ANFANG, HANS-GEORG</au><au>WAGNER, JON, P</au><au>SPIVEY, R., STEVE</au><au>RATNASAMY, CHANDRA</au><format>patent</format><genre>patent</genre><ristype>GEN</ristype><title>A DESULFURIZATION SYSTEM AND METHOD FOR DESULFURIZING A FUEL STREAM</title><date>2013-04-25</date><risdate>2013</risdate><abstract>A method for producing a substantially desulfurized hydrocarbon fuel stream at temperatures less than 100°C. The method includes providing a nondesulfurized fuel cell hydrocarbon fuel stream that may include water and passing the fuel stream through a zeolite Y adsorbent and a selective sulfur adsorbent. The zeolite Y adsorbent may be exchanged with copper ions. The sequence of use depends on the particular sulfur compounds present in the fuel stream. The method produces a substantially desulfurized hydrocarbon fuel stream containing less than 50 ppb sulfur.
Le procédé ci-décrit permet de produire un flux de combustible hydrocarboné essentiellement désulfurisé à des températures inférieures à 100°C. Le procédé comprend l'utilisation d'un flux de combustible hydrocarboné pour pile à combustible non désulfurisé qui peut comprendre de l'eau et le passage du flux de combustible dans un adsorbant du type zéolite Y et dans un adsorbant sélectif de soufre. L'adsorbant de zéolite Y peut être soumis à un échange avec des ions cuivre. La séquence d'utilisation dépend des composés de soufre particuliers présents dans le flux de combustible. Le procédé donne un flux de combustible hydrocarboné essentiellement désulfurisé contenant moins de 50 ppb de soufre.</abstract><oa>free_for_read</oa></addata></record> |
| fulltext | fulltext_linktorsrc |
| identifier | |
| ispartof | |
| issn | |
| language | eng ; fre |
| recordid | cdi_epo_espacenet_WO2010141825A3 |
| source | esp@cenet |
| subjects | CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOIDCHEMISTRY CHEMISTRY CRACKING HYDROCARBON OILS FUELS LUBRICANTS METALLURGY MINERAL WAXES PEAT PERFORMING OPERATIONS PETROLEUM, GAS OR COKE INDUSTRIES PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL 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 SEPARATION TECHNICAL GASES CONTAINING CARBON MONOXIDE THEIR RELEVANT APPARATUS TRANSPORTING |
| title | A DESULFURIZATION SYSTEM AND METHOD FOR DESULFURIZING A FUEL STREAM |
| url | https://sfx.bib-bvb.de/sfx_tum?ctx_ver=Z39.88-2004&ctx_enc=info:ofi/enc:UTF-8&ctx_tim=2025-01-20T02%3A44%3A00IST&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=ANFANG,%20HANS-GEORG&rft.date=2013-04-25&rft_id=info:doi/&rft_dat=%3Cepo_EVB%3EWO2010141825A3%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 |