WO2011056712A3 - Apparatus and process for recovering fcc product - Google Patents

Apparatus and process for recovering fcc product Download PDF

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Publication number
WO2011056712A3
WO2011056712A3 PCT/US2010/054513 US2010054513W WO2011056712A3 WO 2011056712 A3 WO2011056712 A3 WO 2011056712A3 US 2010054513 W US2010054513 W US 2010054513W WO 2011056712 A3 WO2011056712 A3 WO 2011056712A3
Authority
WO
WIPO (PCT)
Prior art keywords
naphtha
recovering
compressor
liquid
unstabilized
Prior art date
Application number
PCT/US2010/054513
Other languages
French (fr)
Other versions
WO2011056712A2 (en
Inventor
Joao J. Da Silva Ferreira Alves
Saadet Ulas Acikgoz
Xin X. Zhu
Laura E. Leonard
Original Assignee
Uop Llc
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
Priority claimed from US12/614,921 external-priority patent/US8231847B2/en
Priority claimed from US12/614,907 external-priority patent/US8414763B2/en
Application filed by Uop Llc filed Critical Uop Llc
Priority to KR1020127011796A priority Critical patent/KR101379539B1/en
Priority to CN2010800504713A priority patent/CN102597179A/en
Publication of WO2011056712A2 publication Critical patent/WO2011056712A2/en
Publication of WO2011056712A3 publication Critical patent/WO2011056712A3/en

Links

Classifications

    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
    • C10G11/00—Catalytic cracking, in the absence of hydrogen, of hydrocarbon oils
    • C10G11/14—Catalytic cracking, in the absence of hydrogen, of hydrocarbon oils with preheated moving solid catalysts
    • C10G11/18—Catalytic cracking, in the absence of hydrogen, of hydrocarbon oils with preheated moving solid catalysts according to the "fluidised-bed" technique
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
    • C10G55/00—Treatment of hydrocarbon oils, in the absence of hydrogen, by at least one refining process and at least one cracking process
    • C10G55/02—Treatment of hydrocarbon oils, in the absence of hydrogen, by at least one refining process and at least one cracking process plural serial stages only
    • C10G55/06—Treatment of hydrocarbon oils, in the absence of hydrogen, by at least one refining process and at least one cracking process plural serial stages only including at least one catalytic cracking step
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
    • C10G70/00—Working-up undefined normally gaseous mixtures obtained by processes covered by groups C10G9/00, C10G11/00, C10G15/00, C10G47/00, C10G51/00
    • C10G70/04—Working-up undefined normally gaseous mixtures obtained by processes covered by groups C10G9/00, C10G11/00, C10G15/00, C10G47/00, C10G51/00 by physical processes
    • C10G70/06—Working-up undefined normally gaseous mixtures obtained by processes covered by groups C10G9/00, C10G11/00, C10G15/00, C10G47/00, C10G51/00 by physical processes by gas-liquid contact
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
    • F25J3/00—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J29/00—Catalysts comprising molecular sieves
    • B01J29/04—Catalysts comprising molecular sieves having base-exchange properties, e.g. crystalline zeolites
    • B01J29/06—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof
    • B01J29/08—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof of the faujasite type, e.g. type X or Y
    • B01J29/084—Y-type faujasite
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J29/00—Catalysts comprising molecular sieves
    • B01J29/04—Catalysts comprising molecular sieves having base-exchange properties, e.g. crystalline zeolites
    • B01J29/06—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof
    • B01J29/40—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof of the pentasil type, e.g. types ZSM-5, ZSM-8 or ZSM-11, as exemplified by patent documents US3702886, GB1334243 and US3709979, respectively
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J29/00—Catalysts comprising molecular sieves
    • B01J29/90—Regeneration or reactivation
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J38/00—Regeneration or reactivation of catalysts, in general
    • B01J38/04—Gas or vapour treating; Treating by using liquids vaporisable upon contacting spent catalyst
    • B01J38/12—Treating with free oxygen-containing gas
    • B01J38/30—Treating with free oxygen-containing gas in gaseous suspension, e.g. fluidised bed
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
    • C10G2300/00—Aspects relating to hydrocarbon processing covered by groups C10G1/00 - C10G99/00
    • C10G2300/10—Feedstock materials
    • C10G2300/1037—Hydrocarbon fractions
    • C10G2300/1044—Heavy gasoline or naphtha having a boiling range of about 100 - 180 °C
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
    • C10G2400/00—Products obtained by processes covered by groups C10G9/00 - C10G69/14
    • C10G2400/20—C2-C4 olefins

Abstract

An apparatus and process are disclosed for recovering product from catalytically converted product streams. Gaseous unstabilized naphtha from an overhead receiver from a main fractionation column is compressed in a compressor. Liquid unstabilized naphtha from the overhead receiver and liquid naphtha fraction from the compressor are sent to a naphtha splitter column upstream of a primary absorber. Consequently, less naphtha is circulated in the gas recovery system.
PCT/US2010/054513 2009-11-09 2010-10-28 Apparatus and process for recovering fcc product WO2011056712A2 (en)

Priority Applications (2)

Application Number Priority Date Filing Date Title
KR1020127011796A KR101379539B1 (en) 2009-11-09 2010-10-28 Apparatus and process for recovering fcc product
CN2010800504713A CN102597179A (en) 2009-11-09 2010-10-28 Apparatus and process for recovering fcc product

Applications Claiming Priority (4)

Application Number Priority Date Filing Date Title
US12/614,921 US8231847B2 (en) 2009-11-09 2009-11-09 Apparatus for recovering FCC product
US12/614,907 2009-11-09
US12/614,921 2009-11-09
US12/614,907 US8414763B2 (en) 2009-11-09 2009-11-09 Process for recovering FCC product

Publications (2)

Publication Number Publication Date
WO2011056712A2 WO2011056712A2 (en) 2011-05-12
WO2011056712A3 true WO2011056712A3 (en) 2011-09-15

Family

ID=43970697

Family Applications (1)

Application Number Title Priority Date Filing Date
PCT/US2010/054513 WO2011056712A2 (en) 2009-11-09 2010-10-28 Apparatus and process for recovering fcc product

Country Status (4)

Country Link
KR (1) KR101379539B1 (en)
CN (1) CN102597179A (en)
SA (1) SA110310847B1 (en)
WO (1) WO2011056712A2 (en)

Families Citing this family (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR2969745B1 (en) 2010-12-27 2013-01-25 Technip France PROCESS FOR PRODUCING METHANE - RICH CURRENT AND CURRENT HYDROCARBON - RICH CURRENT AND ASSOCIATED PLANT.
US9328292B2 (en) * 2013-08-23 2016-05-03 Uop Llc Method and device for improving efficiency of sponge oil absorption
FR3012150B1 (en) 2013-10-23 2016-09-02 Technip France METHOD OF FRACTIONING A CRAB GAS CURRENT USING AN INTERMEDIATE RECYCLE CURRENT, AND ASSOCIATED INSTALLATION
CN105733647B (en) * 2014-12-09 2018-05-01 中科合成油工程股份有限公司 The method that liquefied petroleum gas is recycled from Fischer-Tropsch process exhaust
EP3040405A1 (en) 2014-12-30 2016-07-06 Technip France Method for improving propylene recovery from fluid catalytic cracker unit
WO2017105818A1 (en) * 2015-12-16 2017-06-22 Uop Llc Process for improving propylene recovery from fcc recovery unit
RU2702134C1 (en) * 2019-06-25 2019-10-04 Общество с ограниченной ответственностью "ЭНЕРДЖИ ЭНД ИНЖИНИРИНГ" Method of producing high-octane gasoline fractions
CN115066478A (en) * 2019-12-07 2022-09-16 苏尔寿管理有限公司 Location and cost-effective apparatus and process for separating one or more purified hydrocarbon streams from a crude hydrocarbon stream, such as for naphtha stabilization and LPG recovery

Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4950387A (en) * 1988-10-21 1990-08-21 Mobil Oil Corp. Upgrading of cracking gasoline
US5389237A (en) * 1993-03-08 1995-02-14 Mobil Oil Corporation FCC process with lift gas
US20030094399A1 (en) * 2001-09-28 2003-05-22 Catalytic Distillation Technologies Process for the desulfurization of FCC naphtha
US20060180502A1 (en) * 2005-02-14 2006-08-17 Catalytic Distillation Technologies Process for treating cracked naphtha streams
US20080081937A1 (en) * 2006-09-28 2008-04-03 Schultz Michael A Dividing wall separation in light olefin hydrocarbon processing
US7763165B1 (en) * 2006-12-21 2010-07-27 Uop Llc Fractionation recovery processing of FCC-produced light olefins
US20100247391A1 (en) * 2009-03-31 2010-09-30 Nicholas Christopher P Apparatus for Oligomerizing Dilute Ethylene

Patent Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4950387A (en) * 1988-10-21 1990-08-21 Mobil Oil Corp. Upgrading of cracking gasoline
US5389237A (en) * 1993-03-08 1995-02-14 Mobil Oil Corporation FCC process with lift gas
US20030094399A1 (en) * 2001-09-28 2003-05-22 Catalytic Distillation Technologies Process for the desulfurization of FCC naphtha
US20060180502A1 (en) * 2005-02-14 2006-08-17 Catalytic Distillation Technologies Process for treating cracked naphtha streams
US20080081937A1 (en) * 2006-09-28 2008-04-03 Schultz Michael A Dividing wall separation in light olefin hydrocarbon processing
US7763165B1 (en) * 2006-12-21 2010-07-27 Uop Llc Fractionation recovery processing of FCC-produced light olefins
US20100247391A1 (en) * 2009-03-31 2010-09-30 Nicholas Christopher P Apparatus for Oligomerizing Dilute Ethylene

Also Published As

Publication number Publication date
WO2011056712A2 (en) 2011-05-12
SA110310847B1 (en) 2014-04-14
KR101379539B1 (en) 2014-03-28
KR20120080237A (en) 2012-07-16
CN102597179A (en) 2012-07-18

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