PROCESS FOR MIXING DILUTION STEAM WITH LIQUID HYDROCARBONS BEFORE STEAM CRACKING
상대적으로 큰 탄화수소 액적 크기를 유지하는 휘발 단계를 포함하는 전체 원유를 증기 분해하는 공정이 수행된다. 공정은 전체 원유를 증기와 접촉시켜서 탄화수소의 일부를 증발시키는 단계를 포함할 수 있고, 여기서 탄화수소 공급원료 및 증기를 증발시키는 단계는 예를 들어, 30 m/s 미만의 초기 상대 속도에서 진행될 수 있다. 생성되는 기상은 증발된 탄화수소 및 증기를 포함하고, 비증발된 탄화수소를 포함하는 액상으로부터 분리될 수 있다. 기상 탄화수소는 기상의 탄화수소를 증기 분해하는 증기 열분해 반응기로 보내질 수 있다. Proces...
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| creator | NARAYAN RAGHU AKHRAS ABDUL RAHMAN ZAFER MALONEY DENNIS SUNDARAM KANDASAMY |
| description | 상대적으로 큰 탄화수소 액적 크기를 유지하는 휘발 단계를 포함하는 전체 원유를 증기 분해하는 공정이 수행된다. 공정은 전체 원유를 증기와 접촉시켜서 탄화수소의 일부를 증발시키는 단계를 포함할 수 있고, 여기서 탄화수소 공급원료 및 증기를 증발시키는 단계는 예를 들어, 30 m/s 미만의 초기 상대 속도에서 진행될 수 있다. 생성되는 기상은 증발된 탄화수소 및 증기를 포함하고, 비증발된 탄화수소를 포함하는 액상으로부터 분리될 수 있다. 기상 탄화수소는 기상의 탄화수소를 증기 분해하는 증기 열분해 반응기로 보내질 수 있다.
Processes herein may be used to thermally crack various hydrocarbon feeds, and may eliminate the refinery altogether while making the crude to chemicals process very flexible in terms of crude. In embodiments herein, crude is progressively separated into at least light and heavy fractions. Depending on the quality of the light and heavy fractions, these are routed to one of three upgrading operations, including a fixed bed hydroconversion unit, a fluidized catalytic conversion unit, or a residue hydrocracking unit that may utilize an ebullated bed reactor. Products from the upgrading operations may be used as feed to a steam cracker. |
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Processes herein may be used to thermally crack various hydrocarbon feeds, and may eliminate the refinery altogether while making the crude to chemicals process very flexible in terms of crude. In embodiments herein, crude is progressively separated into at least light and heavy fractions. Depending on the quality of the light and heavy fractions, these are routed to one of three upgrading operations, including a fixed bed hydroconversion unit, a fluidized catalytic conversion unit, or a residue hydrocracking unit that may utilize an ebullated bed reactor. Products from the upgrading operations may be used as feed to a steam cracker.</description><language>eng ; kor</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>2024</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=20241119&DB=EPODOC&CC=KR&NR=20240164592A$$EHTML$$P50$$Gepo$$Hfree_for_read</linktohtml><link.rule.ids>230,308,780,885,25563,76318</link.rule.ids><linktorsrc>$$Uhttps://worldwide.espacenet.com/publicationDetails/biblio?FT=D&date=20241119&DB=EPODOC&CC=KR&NR=20240164592A$$EView_record_in_European_Patent_Office$$FView_record_in_$$GEuropean_Patent_Office$$Hfree_for_read</linktorsrc></links><search><creatorcontrib>NARAYAN RAGHU</creatorcontrib><creatorcontrib>AKHRAS ABDUL RAHMAN ZAFER</creatorcontrib><creatorcontrib>MALONEY DENNIS</creatorcontrib><creatorcontrib>SUNDARAM KANDASAMY</creatorcontrib><title>PROCESS FOR MIXING DILUTION STEAM WITH LIQUID HYDROCARBONS BEFORE STEAM CRACKING</title><description>상대적으로 큰 탄화수소 액적 크기를 유지하는 휘발 단계를 포함하는 전체 원유를 증기 분해하는 공정이 수행된다. 공정은 전체 원유를 증기와 접촉시켜서 탄화수소의 일부를 증발시키는 단계를 포함할 수 있고, 여기서 탄화수소 공급원료 및 증기를 증발시키는 단계는 예를 들어, 30 m/s 미만의 초기 상대 속도에서 진행될 수 있다. 생성되는 기상은 증발된 탄화수소 및 증기를 포함하고, 비증발된 탄화수소를 포함하는 액상으로부터 분리될 수 있다. 기상 탄화수소는 기상의 탄화수소를 증기 분해하는 증기 열분해 반응기로 보내질 수 있다.
Processes herein may be used to thermally crack various hydrocarbon feeds, and may eliminate the refinery altogether while making the crude to chemicals process very flexible in terms of crude. In embodiments herein, crude is progressively separated into at least light and heavy fractions. Depending on the quality of the light and heavy fractions, these are routed to one of three upgrading operations, including a fixed bed hydroconversion unit, a fluidized catalytic conversion unit, or a residue hydrocracking unit that may utilize an ebullated bed reactor. Products from the upgrading operations may be used as feed to a steam cracker.</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>2024</creationdate><recordtype>patent</recordtype><sourceid>EVB</sourceid><recordid>eNrjZAgICPJ3dg0OVnDzD1Lw9Yzw9HNXcPH0CQ3x9PdTCA5xdfRVCPcM8VDw8QwM9XRR8Ih0Aap3DHLy9wtWcHIFanKFqnIOcnT2BurmYWBNS8wpTuWF0twMym6uIc4euqkF-fGpxQWJyal5qSXx3kFGBkYmBoZmJqaWRo7GxKkCAEV1MA4</recordid><startdate>20241119</startdate><enddate>20241119</enddate><creator>NARAYAN RAGHU</creator><creator>AKHRAS ABDUL RAHMAN ZAFER</creator><creator>MALONEY DENNIS</creator><creator>SUNDARAM KANDASAMY</creator><scope>EVB</scope></search><sort><creationdate>20241119</creationdate><title>PROCESS FOR MIXING DILUTION STEAM WITH LIQUID HYDROCARBONS BEFORE STEAM CRACKING</title><author>NARAYAN RAGHU ; AKHRAS ABDUL RAHMAN ZAFER ; MALONEY DENNIS ; SUNDARAM KANDASAMY</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-epo_espacenet_KR20240164592A3</frbrgroupid><rsrctype>patents</rsrctype><prefilter>patents</prefilter><language>eng ; kor</language><creationdate>2024</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>NARAYAN RAGHU</creatorcontrib><creatorcontrib>AKHRAS ABDUL RAHMAN ZAFER</creatorcontrib><creatorcontrib>MALONEY DENNIS</creatorcontrib><creatorcontrib>SUNDARAM KANDASAMY</creatorcontrib><collection>esp@cenet</collection></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext_linktorsrc</fulltext></delivery><addata><au>NARAYAN RAGHU</au><au>AKHRAS ABDUL RAHMAN ZAFER</au><au>MALONEY DENNIS</au><au>SUNDARAM KANDASAMY</au><format>patent</format><genre>patent</genre><ristype>GEN</ristype><title>PROCESS FOR MIXING DILUTION STEAM WITH LIQUID HYDROCARBONS BEFORE STEAM CRACKING</title><date>2024-11-19</date><risdate>2024</risdate><abstract>상대적으로 큰 탄화수소 액적 크기를 유지하는 휘발 단계를 포함하는 전체 원유를 증기 분해하는 공정이 수행된다. 공정은 전체 원유를 증기와 접촉시켜서 탄화수소의 일부를 증발시키는 단계를 포함할 수 있고, 여기서 탄화수소 공급원료 및 증기를 증발시키는 단계는 예를 들어, 30 m/s 미만의 초기 상대 속도에서 진행될 수 있다. 생성되는 기상은 증발된 탄화수소 및 증기를 포함하고, 비증발된 탄화수소를 포함하는 액상으로부터 분리될 수 있다. 기상 탄화수소는 기상의 탄화수소를 증기 분해하는 증기 열분해 반응기로 보내질 수 있다.
Processes herein may be used to thermally crack various hydrocarbon feeds, and may eliminate the refinery altogether while making the crude to chemicals process very flexible in terms of crude. In embodiments herein, crude is progressively separated into at least light and heavy fractions. Depending on the quality of the light and heavy fractions, these are routed to one of three upgrading operations, including a fixed bed hydroconversion unit, a fluidized catalytic conversion unit, or a residue hydrocracking unit that may utilize an ebullated bed reactor. Products from the upgrading operations may be used as feed to a steam cracker.</abstract><oa>free_for_read</oa></addata></record> |
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| 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 | PROCESS FOR MIXING DILUTION STEAM WITH LIQUID HYDROCARBONS BEFORE STEAM CRACKING |
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