FLUIDIZED CATALYTIC CONVERSION METHOD FOR MAXIMIZING PRODUCTION OF PROPYLENE
Disclosed is a fluidized catalytic conversion method for maximizing the production of propylene, comprising the steps of: 1) contacting a heavy feedstock oil with a catalytic conversion catalyst having a temperature of 650 °C or higher for reaction; 2) contacting a hydrocarbon oil feedstock having a...
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Format | Patent |
Language | English French German |
Published |
01.11.2023
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Abstract | Disclosed is a fluidized catalytic conversion method for maximizing the production of propylene, comprising the steps of: 1) contacting a heavy feedstock oil with a catalytic conversion catalyst having a temperature of 650 °C or higher for reaction; 2) contacting a hydrocarbon oil feedstock having an olefin content of 50 wt% or more with the catalytic conversion catalyst after the reaction of step 1); 3) separating a first catalytic cracking distillate oil and a second catalytic cracking distillate oil from the resulting reaction products; 4) separating an olefin-rich stream from the first catalytic cracking distillate oil; and 5) recycling the olefin-rich stream. The method can effectively improve the yield of propylene and realize an effective utilization of petroleum resources. |
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AbstractList | Disclosed is a fluidized catalytic conversion method for maximizing the production of propylene, comprising the steps of: 1) contacting a heavy feedstock oil with a catalytic conversion catalyst having a temperature of 650 °C or higher for reaction; 2) contacting a hydrocarbon oil feedstock having an olefin content of 50 wt% or more with the catalytic conversion catalyst after the reaction of step 1); 3) separating a first catalytic cracking distillate oil and a second catalytic cracking distillate oil from the resulting reaction products; 4) separating an olefin-rich stream from the first catalytic cracking distillate oil; and 5) recycling the olefin-rich stream. The method can effectively improve the yield of propylene and realize an effective utilization of petroleum resources. |
Author | WANG, Xieqing ZHANG, Yunpeng SHU, Xingtian LUO, Yibin HAN, Yueyang DU, Lingyin XU, Youhao ZUO, Yanfen |
Author_xml | – fullname: LUO, Yibin – fullname: DU, Lingyin – fullname: XU, Youhao – fullname: HAN, Yueyang – fullname: SHU, Xingtian – fullname: WANG, Xieqing – fullname: ZUO, Yanfen – fullname: ZHANG, Yunpeng |
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DocumentTitleAlternate | FLUIDISIERTES KATALYTISCHES UMWANDLUNGSVERFAHREN ZUR MAXIMIERUNG DER HERSTELLUNG VON PROPYLEN PROCÉDÉ DE CONVERSION CATALYTIQUE FLUIDISÉE POUR AUGMENTER AU MAXIMUM LA PRODUCTION DE PROPYLÈNE |
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Notes | Application Number: EP20210917017 |
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RelatedCompanies | China Petroleum & Chemical Corporation Sinopec Research Institute of Petroleum Processing Co., Ltd |
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Snippet | Disclosed is a fluidized catalytic conversion method for maximizing the production of propylene, comprising the steps of: 1) contacting a heavy feedstock oil... |
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SubjectTerms | ACYCLIC OR CARBOCYCLIC COMPOUNDS CHEMISTRY CRACKING HYDROCARBON OILS FUELS 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 | FLUIDIZED CATALYTIC CONVERSION METHOD FOR MAXIMIZING PRODUCTION OF PROPYLENE |
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