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WO2011051434A3 - Cracking process - Google Patents

Cracking process
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Publication number
WO2011051434A3
WO2011051434A3PCT/EP2010/066450EP2010066450WWO2011051434A3WO 2011051434 A3WO2011051434 A3WO 2011051434A3EP 2010066450 WEP2010066450 WEP 2010066450WWO 2011051434 A3WO2011051434 A3WO 2011051434A3
Authority
WO
WIPO (PCT)
Prior art keywords
separating
product
carbon atoms
fractions
feed
Prior art date
Application number
PCT/EP2010/066450
Other languages
French (fr)
Other versions
WO2011051434A2 (en
Inventor
John William Harris
Original Assignee
Shell Internationale Research Maatschappij B.V.
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Shell Internationale Research Maatschappij B.V.filedCriticalShell Internationale Research Maatschappij B.V.
Publication of WO2011051434A2publicationCriticalpatent/WO2011051434A2/en
Publication of WO2011051434A3publicationCriticalpatent/WO2011051434A3/en

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Abstract

Process for converting a hydrocarbon feed which process comprises (a) catalytically cracking the feed, (b) separating the mixture obtained in step (a) into spent catalyst and hydrocarbon product, (c) separating the hydrocarbon product of step (b) into two or more fractions, (d) further catalytically cracking at least one of the fractions obtained in step (c), (e) separating the mixture obtained in step (d) into used catalyst and hydrocarbon product, (f) subjecting one or more fractions obtained in step (c) and hydrocarbon product of step (e) to separation such as to obtain a gas and one or more liquid fractions, (g) increasing the pressure of the gas obtained in step (f), (h) separating hydrocarbons comprising 3 carbon atoms from the product of step (g) to obtain propane-lean product, and (i) separating the propane-lean product obtained in step (h) into a fraction containing hydrocarbons comprising 4 carbon atoms, a fraction containing hydrocarbons comprising 5 or 6 carbon atoms, and a heavy fraction, in which process the fraction containing hydrocarbons comprising 5 or 6 carbon atoms obtained in step (i) is sent as feed to step (d).
PCT/EP2010/0664502009-11-022010-10-29Cracking processWO2011051434A2 (en)

Applications Claiming Priority (2)

Application NumberPriority DateFiling DateTitle
EP091747362009-11-02
EP09174736.02009-11-02

Publications (2)

Publication NumberPublication Date
WO2011051434A2 WO2011051434A2 (en)2011-05-05
WO2011051434A3true WO2011051434A3 (en)2011-07-14

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ID=42026548

Family Applications (1)

Application NumberTitlePriority DateFiling Date
PCT/EP2010/066450WO2011051434A2 (en)2009-11-022010-10-29Cracking process

Country Status (1)

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WO (1)WO2011051434A2 (en)

Citations (5)

* Cited by examiner, † Cited by third party
Publication numberPriority datePublication dateAssigneeTitle
US3974062A (en)*1974-10-171976-08-10Mobil Oil CorporationConversion of full range crude oils with low molecular weight carbon-hydrogen fragment contributors over zeolite catalysts
US4090949A (en)*1974-07-311978-05-23Mobil Oil CorportionUpgrading of olefinic gasoline with hydrogen contributors
EP0382289A1 (en)*1989-02-061990-08-16Stone & Webster Engineering CorporationProcess for catalytic cracking of hydrocarbons
US5087349A (en)*1988-11-181992-02-11Stone & Webster Engineering CorporationProcess for selectively maximizing product production in fluidized catalytic cracking of hydrocarbons
WO2001060951A1 (en)*2000-02-162001-08-23Indian Oil Corporation LimitedA multi stage selective catalytic cracking process and a system for producing high yield of middle distillate products from heavy hydrocarbon feedstocks

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication numberPriority datePublication dateAssigneeTitle
US4090949A (en)*1974-07-311978-05-23Mobil Oil CorportionUpgrading of olefinic gasoline with hydrogen contributors
US3974062A (en)*1974-10-171976-08-10Mobil Oil CorporationConversion of full range crude oils with low molecular weight carbon-hydrogen fragment contributors over zeolite catalysts
US5087349A (en)*1988-11-181992-02-11Stone & Webster Engineering CorporationProcess for selectively maximizing product production in fluidized catalytic cracking of hydrocarbons
EP0382289A1 (en)*1989-02-061990-08-16Stone & Webster Engineering CorporationProcess for catalytic cracking of hydrocarbons
WO2001060951A1 (en)*2000-02-162001-08-23Indian Oil Corporation LimitedA multi stage selective catalytic cracking process and a system for producing high yield of middle distillate products from heavy hydrocarbon feedstocks

Also Published As

Publication numberPublication date
WO2011051434A2 (en)2011-05-05

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