DEWAXING CATALYSTS AND PROCESSES USING THE SAME
Provided herein are catalysts for dewaxing of a feedstock, the catalyst comprising between about 40 wt.% and about 99.9 wt.% zeolite, between about 0 wt.% and about 40 wt.% binder and at least about 0.1 wt.% noble metal, as well as catalyst systems, methods and products produced using the catalysts....
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| creator | KNAEBLE, William WEIGEL, Scott KAMAKOTI, Preeti |
| description | Provided herein are catalysts for dewaxing of a feedstock, the catalyst comprising between about 40 wt.% and about 99.9 wt.% zeolite, between about 0 wt.% and about 40 wt.% binder and at least about 0.1 wt.% noble metal, as well as catalyst systems, methods and products produced using the catalysts. The zeolite having a crystal comprising a largest included sphere less than or equal to about 7,5 angstroms, a largest diffusing sphere greater than or equal to about 5.0 angstroms, and a silica to alumina ratio greater than or equal to about 100:1. The catalyst having a temperature-programmed ammonia desorption ("TPAD") of less than about 0.25 mmol/g.
L'invention concerne des catalyseurs pour le déparaffinage d'une matière première, le catalyseur comprenant entre environ 40 % en poids et environ 99,9 % en poids de zéolite, entre environ 0 % en poids et environ 40 % en poids de liant et au moins environ 0,1 % en poids de métal noble, ainsi que des systèmes, des procédés et des produits de catalyseur produits en utilisant les catalyseurs. La zéolite ayant un cristal comprenant une sphère incluse la plus grande inférieure ou égale à environ 7,5 angströms, une sphère diffusante la plus grande supérieure ou égale à environ 5,0 angströms, et un rapport silice/alumine supérieur ou égal à environ 100:1. Le catalyseur ayant une désorption d'ammoniac programmée en température ("TPAD") inférieure à environ 0,25 mmol/g. |
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L'invention concerne des catalyseurs pour le déparaffinage d'une matière première, le catalyseur comprenant entre environ 40 % en poids et environ 99,9 % en poids de zéolite, entre environ 0 % en poids et environ 40 % en poids de liant et au moins environ 0,1 % en poids de métal noble, ainsi que des systèmes, des procédés et des produits de catalyseur produits en utilisant les catalyseurs. La zéolite ayant un cristal comprenant une sphère incluse la plus grande inférieure ou égale à environ 7,5 angströms, une sphère diffusante la plus grande supérieure ou égale à environ 5,0 angströms, et un rapport silice/alumine supérieur ou égal à environ 100:1. Le catalyseur ayant une désorption d'ammoniac programmée en température ("TPAD") inférieure à environ 0,25 mmol/g.</description><language>eng ; fre</language><subject>ACYCLIC OR CARBOCYCLIC COMPOUNDS ; CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOIDCHEMISTRY ; CHEMISTRY ; CRACKING HYDROCARBON OILS ; FUELS ; LUBRICANTS ; METALLURGY ; MINERAL WAXES ; ORGANIC CHEMISTRY ; 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 ; TECHNICAL GASES CONTAINING CARBON MONOXIDE ; THEIR RELEVANT APPARATUS ; TRANSPORTING</subject><creationdate>2022</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=20220811&DB=EPODOC&CC=WO&NR=2022170298A1$$EHTML$$P50$$Gepo$$Hfree_for_read</linktohtml><link.rule.ids>230,308,780,885,25564,76547</link.rule.ids><linktorsrc>$$Uhttps://worldwide.espacenet.com/publicationDetails/biblio?FT=D&date=20220811&DB=EPODOC&CC=WO&NR=2022170298A1$$EView_record_in_European_Patent_Office$$FView_record_in_$$GEuropean_Patent_Office$$Hfree_for_read</linktorsrc></links><search><creatorcontrib>KNAEBLE, William</creatorcontrib><creatorcontrib>WEIGEL, Scott</creatorcontrib><creatorcontrib>KAMAKOTI, Preeti</creatorcontrib><title>DEWAXING CATALYSTS AND PROCESSES USING THE SAME</title><description>Provided herein are catalysts for dewaxing of a feedstock, the catalyst comprising between about 40 wt.% and about 99.9 wt.% zeolite, between about 0 wt.% and about 40 wt.% binder and at least about 0.1 wt.% noble metal, as well as catalyst systems, methods and products produced using the catalysts. The zeolite having a crystal comprising a largest included sphere less than or equal to about 7,5 angstroms, a largest diffusing sphere greater than or equal to about 5.0 angstroms, and a silica to alumina ratio greater than or equal to about 100:1. The catalyst having a temperature-programmed ammonia desorption ("TPAD") of less than about 0.25 mmol/g.
L'invention concerne des catalyseurs pour le déparaffinage d'une matière première, le catalyseur comprenant entre environ 40 % en poids et environ 99,9 % en poids de zéolite, entre environ 0 % en poids et environ 40 % en poids de liant et au moins environ 0,1 % en poids de métal noble, ainsi que des systèmes, des procédés et des produits de catalyseur produits en utilisant les catalyseurs. La zéolite ayant un cristal comprenant une sphère incluse la plus grande inférieure ou égale à environ 7,5 angströms, une sphère diffusante la plus grande supérieure ou égale à environ 5,0 angströms, et un rapport silice/alumine supérieur ou égal à environ 100:1. Le catalyseur ayant une désorption d'ammoniac programmée en température ("TPAD") inférieure à environ 0,25 mmol/g.</description><subject>ACYCLIC OR CARBOCYCLIC COMPOUNDS</subject><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>ORGANIC CHEMISTRY</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>TECHNICAL GASES CONTAINING CARBON MONOXIDE</subject><subject>THEIR RELEVANT APPARATUS</subject><subject>TRANSPORTING</subject><fulltext>true</fulltext><rsrctype>patent</rsrctype><creationdate>2022</creationdate><recordtype>patent</recordtype><sourceid>EVB</sourceid><recordid>eNrjZNB3cQ13jPD0c1dwdgxx9IkMDglWcPRzUQgI8nd2DQ52DVYIDQbJhni4KgQ7-rryMLCmJeYUp_JCaW4GZTfXEGcP3dSC_PjU4oLE5NS81JL4cH8jAyMjQ3MDI0sLR0Nj4lQBAKKcJu4</recordid><startdate>20220811</startdate><enddate>20220811</enddate><creator>KNAEBLE, William</creator><creator>WEIGEL, Scott</creator><creator>KAMAKOTI, Preeti</creator><scope>EVB</scope></search><sort><creationdate>20220811</creationdate><title>DEWAXING CATALYSTS AND PROCESSES USING THE SAME</title><author>KNAEBLE, William ; WEIGEL, Scott ; KAMAKOTI, Preeti</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-epo_espacenet_WO2022170298A13</frbrgroupid><rsrctype>patents</rsrctype><prefilter>patents</prefilter><language>eng ; fre</language><creationdate>2022</creationdate><topic>ACYCLIC OR CARBOCYCLIC COMPOUNDS</topic><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>ORGANIC CHEMISTRY</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>TECHNICAL GASES CONTAINING CARBON MONOXIDE</topic><topic>THEIR RELEVANT APPARATUS</topic><topic>TRANSPORTING</topic><toplevel>online_resources</toplevel><creatorcontrib>KNAEBLE, William</creatorcontrib><creatorcontrib>WEIGEL, Scott</creatorcontrib><creatorcontrib>KAMAKOTI, Preeti</creatorcontrib><collection>esp@cenet</collection></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext_linktorsrc</fulltext></delivery><addata><au>KNAEBLE, William</au><au>WEIGEL, Scott</au><au>KAMAKOTI, Preeti</au><format>patent</format><genre>patent</genre><ristype>GEN</ristype><title>DEWAXING CATALYSTS AND PROCESSES USING THE SAME</title><date>2022-08-11</date><risdate>2022</risdate><abstract>Provided herein are catalysts for dewaxing of a feedstock, the catalyst comprising between about 40 wt.% and about 99.9 wt.% zeolite, between about 0 wt.% and about 40 wt.% binder and at least about 0.1 wt.% noble metal, as well as catalyst systems, methods and products produced using the catalysts. The zeolite having a crystal comprising a largest included sphere less than or equal to about 7,5 angstroms, a largest diffusing sphere greater than or equal to about 5.0 angstroms, and a silica to alumina ratio greater than or equal to about 100:1. The catalyst having a temperature-programmed ammonia desorption ("TPAD") of less than about 0.25 mmol/g.
L'invention concerne des catalyseurs pour le déparaffinage d'une matière première, le catalyseur comprenant entre environ 40 % en poids et environ 99,9 % en poids de zéolite, entre environ 0 % en poids et environ 40 % en poids de liant et au moins environ 0,1 % en poids de métal noble, ainsi que des systèmes, des procédés et des produits de catalyseur produits en utilisant les catalyseurs. La zéolite ayant un cristal comprenant une sphère incluse la plus grande inférieure ou égale à environ 7,5 angströms, une sphère diffusante la plus grande supérieure ou égale à environ 5,0 angströms, et un rapport silice/alumine supérieur ou égal à environ 100:1. Le catalyseur ayant une désorption d'ammoniac programmée en température ("TPAD") inférieure à environ 0,25 mmol/g.</abstract><oa>free_for_read</oa></addata></record> |
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| subjects | ACYCLIC OR CARBOCYCLIC COMPOUNDS CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOIDCHEMISTRY CHEMISTRY CRACKING HYDROCARBON OILS FUELS LUBRICANTS METALLURGY MINERAL WAXES ORGANIC CHEMISTRY 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 TECHNICAL GASES CONTAINING CARBON MONOXIDE THEIR RELEVANT APPARATUS TRANSPORTING |
| title | DEWAXING CATALYSTS AND PROCESSES USING THE SAME |
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