MULTI-TUBE REACTOR SYSTEMS AND PROCESSES FOR NO-OXIDATIVE CONVERSION OF METHANE
The present disclosure refers to systems and methods for efficiently converting a C1-C3 alkane such as natural gas to a liquid C2-C10 product and hydrogen. Generally, the process comprises flowing the C1-C3 alkane through a plurality of tubes within a vessel wherein the tubes house a catalyst for co...
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| creator | LI, Lin LUO, Huping OUYANG, Xiaoying KUPERMAN, Alexander |
| description | The present disclosure refers to systems and methods for efficiently converting a C1-C3 alkane such as natural gas to a liquid C2-C10 product and hydrogen. Generally, the process comprises flowing the C1-C3 alkane through a plurality of tubes within a vessel wherein the tubes house a catalyst for converting the C1-C3 alkane to the liquid C2-C10 product and hydrogen. The C1- C3 alkane is heated under suitable conditions to produce the liquid C2-C10 product and hydrogen. Advantageously, the C1-C3 alkane is heated by burning a fuel outside the tubes in fuel burning nozzles configured to transfer heat from the burning through the tubes.
La présente divulgation concerne des systèmes et des procédés pour convertir de manière efficace un alcane en C1-C3 tel qu'un gaz naturel en un produit liquide en C2-C10 et de l'hydrogène. D'une manière générale, le procédé comprend la mise en écoulement de l'alcane en C1-C3 à travers une pluralité de tubes à l'intérieur d'un récipient, les tubes comprenant un catalyseur destiné à convertir l'alcane en C1-C3 en produit liquide en C2-C10 et en hydrogène. L'alcane en C1-C3 est chauffé dans des conditions appropriées pour produire le produit liquide en C2-C10 et de l'hydrogène. Avantageusement, l'alcane en C1-C3 est chauffé par combustion d'un combustible à l'extérieur des tubes dans des buses de combustion de combustible conçues pour transférer la chaleur de combustion à travers les tubes. |
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La présente divulgation concerne des systèmes et des procédés pour convertir de manière efficace un alcane en C1-C3 tel qu'un gaz naturel en un produit liquide en C2-C10 et de l'hydrogène. D'une manière générale, le procédé comprend la mise en écoulement de l'alcane en C1-C3 à travers une pluralité de tubes à l'intérieur d'un récipient, les tubes comprenant un catalyseur destiné à convertir l'alcane en C1-C3 en produit liquide en C2-C10 et en hydrogène. L'alcane en C1-C3 est chauffé dans des conditions appropriées pour produire le produit liquide en C2-C10 et de l'hydrogène. Avantageusement, l'alcane en C1-C3 est chauffé par combustion d'un combustible à l'extérieur des tubes dans des buses de combustion de combustible conçues pour transférer la chaleur de combustion à travers les tubes.</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>2023</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=20230907&DB=EPODOC&CC=WO&NR=2023167929A1$$EHTML$$P50$$Gepo$$Hfree_for_read</linktohtml><link.rule.ids>230,308,780,885,25564,76547</link.rule.ids><linktorsrc>$$Uhttps://worldwide.espacenet.com/publicationDetails/biblio?FT=D&date=20230907&DB=EPODOC&CC=WO&NR=2023167929A1$$EView_record_in_European_Patent_Office$$FView_record_in_$$GEuropean_Patent_Office$$Hfree_for_read</linktorsrc></links><search><creatorcontrib>LI, Lin</creatorcontrib><creatorcontrib>LUO, Huping</creatorcontrib><creatorcontrib>OUYANG, Xiaoying</creatorcontrib><creatorcontrib>KUPERMAN, Alexander</creatorcontrib><title>MULTI-TUBE REACTOR SYSTEMS AND PROCESSES FOR NO-OXIDATIVE CONVERSION OF METHANE</title><description>The present disclosure refers to systems and methods for efficiently converting a C1-C3 alkane such as natural gas to a liquid C2-C10 product and hydrogen. Generally, the process comprises flowing the C1-C3 alkane through a plurality of tubes within a vessel wherein the tubes house a catalyst for converting the C1-C3 alkane to the liquid C2-C10 product and hydrogen. The C1- C3 alkane is heated under suitable conditions to produce the liquid C2-C10 product and hydrogen. Advantageously, the C1-C3 alkane is heated by burning a fuel outside the tubes in fuel burning nozzles configured to transfer heat from the burning through the tubes.
La présente divulgation concerne des systèmes et des procédés pour convertir de manière efficace un alcane en C1-C3 tel qu'un gaz naturel en un produit liquide en C2-C10 et de l'hydrogène. D'une manière générale, le procédé comprend la mise en écoulement de l'alcane en C1-C3 à travers une pluralité de tubes à l'intérieur d'un récipient, les tubes comprenant un catalyseur destiné à convertir l'alcane en C1-C3 en produit liquide en C2-C10 et en hydrogène. L'alcane en C1-C3 est chauffé dans des conditions appropriées pour produire le produit liquide en C2-C10 et de l'hydrogène. Avantageusement, l'alcane en C1-C3 est chauffé par combustion d'un combustible à l'extérieur des tubes dans des buses de combustion de combustible conçues pour transférer la chaleur de combustion à travers les tubes.</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>2023</creationdate><recordtype>patent</recordtype><sourceid>EVB</sourceid><recordid>eNqNyrEKwjAQgOEuDqK-w4FzwLagdIzphQZMTnLXVqdSJE6ihfr-6OADOP3D9y8z8u1JnJL2iBBRG6EIfGVBz6BDDedIBpmRwX4lkKKLq7W4DsFQ6DCyowBkwaM0OuA6W9zHx5w2v66yrUUxjUrTa0jzNN7SM72HnopdUeb7Q1VUOi__uz4ryDAN</recordid><startdate>20230907</startdate><enddate>20230907</enddate><creator>LI, Lin</creator><creator>LUO, Huping</creator><creator>OUYANG, Xiaoying</creator><creator>KUPERMAN, Alexander</creator><scope>EVB</scope></search><sort><creationdate>20230907</creationdate><title>MULTI-TUBE REACTOR SYSTEMS AND PROCESSES FOR NO-OXIDATIVE CONVERSION OF METHANE</title><author>LI, Lin ; LUO, Huping ; OUYANG, Xiaoying ; KUPERMAN, Alexander</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-epo_espacenet_WO2023167929A13</frbrgroupid><rsrctype>patents</rsrctype><prefilter>patents</prefilter><language>eng ; fre</language><creationdate>2023</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>LI, Lin</creatorcontrib><creatorcontrib>LUO, Huping</creatorcontrib><creatorcontrib>OUYANG, Xiaoying</creatorcontrib><creatorcontrib>KUPERMAN, Alexander</creatorcontrib><collection>esp@cenet</collection></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext_linktorsrc</fulltext></delivery><addata><au>LI, Lin</au><au>LUO, Huping</au><au>OUYANG, Xiaoying</au><au>KUPERMAN, Alexander</au><format>patent</format><genre>patent</genre><ristype>GEN</ristype><title>MULTI-TUBE REACTOR SYSTEMS AND PROCESSES FOR NO-OXIDATIVE CONVERSION OF METHANE</title><date>2023-09-07</date><risdate>2023</risdate><abstract>The present disclosure refers to systems and methods for efficiently converting a C1-C3 alkane such as natural gas to a liquid C2-C10 product and hydrogen. Generally, the process comprises flowing the C1-C3 alkane through a plurality of tubes within a vessel wherein the tubes house a catalyst for converting the C1-C3 alkane to the liquid C2-C10 product and hydrogen. The C1- C3 alkane is heated under suitable conditions to produce the liquid C2-C10 product and hydrogen. Advantageously, the C1-C3 alkane is heated by burning a fuel outside the tubes in fuel burning nozzles configured to transfer heat from the burning through the tubes.
La présente divulgation concerne des systèmes et des procédés pour convertir de manière efficace un alcane en C1-C3 tel qu'un gaz naturel en un produit liquide en C2-C10 et de l'hydrogène. D'une manière générale, le procédé comprend la mise en écoulement de l'alcane en C1-C3 à travers une pluralité de tubes à l'intérieur d'un récipient, les tubes comprenant un catalyseur destiné à convertir l'alcane en C1-C3 en produit liquide en C2-C10 et en hydrogène. L'alcane en C1-C3 est chauffé dans des conditions appropriées pour produire le produit liquide en C2-C10 et de l'hydrogène. Avantageusement, l'alcane en C1-C3 est chauffé par combustion d'un combustible à l'extérieur des tubes dans des buses de combustion de combustible conçues pour transférer la chaleur de combustion à travers les tubes.</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 | MULTI-TUBE REACTOR SYSTEMS AND PROCESSES FOR NO-OXIDATIVE CONVERSION OF METHANE |
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