ATE142247T1 - DRAIN EXTRACTION DEVICE CONTAINING DISSIPATION PLATES FOR FCC PROCESSES - Google Patents
DRAIN EXTRACTION DEVICE CONTAINING DISSIPATION PLATES FOR FCC PROCESSESInfo
- Publication number
- ATE142247T1 ATE142247T1 AT92309716T AT92309716T ATE142247T1 AT E142247 T1 ATE142247 T1 AT E142247T1 AT 92309716 T AT92309716 T AT 92309716T AT 92309716 T AT92309716 T AT 92309716T AT E142247 T1 ATE142247 T1 AT E142247T1
- Authority
- AT
- Austria
- Prior art keywords
- catalyst
- disengaging vessel
- outlet
- vessel
- extraction device
- Prior art date
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
Abstract
A method and apparatus for an FCC process uses dissipator plates at the outlet of a disengaging vessel to provide a quick separation of catalyst from product vapors and to prevent reentrainment of catalyst by stripping gas which is passed into the disengaging vessel. The process and apparatus use a riser for the conversion of an FCC feedstock and direct the effluent from the riser directly into a disengaging vessel to separate catalyst from the product vapors. Catalyst is directed downwardly out of the outlet of the disengaging vessel and through a series of dissipator plates that eliminate the tangential velocity that would be otherwise introduced by the vortex and would lead to reentrainment of catalyst. The dissipator plates are located in a stripping vessel positioned immediately below the disengaging vessel outlet to receive catalyst as it leaves the disengaging vessel. <IMAGE>
Applications Claiming Priority (7)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US07/613,037 US5158669A (en) | 1990-11-15 | 1990-11-15 | Disengager stripper |
CA002080974A CA2080974C (en) | 1990-11-15 | 1992-10-20 | Disengager stripper containing dissipation plates for use in an fcc process |
AU27278/92A AU649889B1 (en) | 1990-11-15 | 1992-10-21 | Disengager stripper containing dissipation plates for use in an FCC process |
EP92309716A EP0593827B1 (en) | 1990-11-15 | 1992-10-23 | Disengager stripper containing dissipation plates for use in an FCC process |
CN92112441A CN1035773C (en) | 1990-11-15 | 1992-10-26 | Disengager stripper containing dissipation plates for use in an FCC process |
US07/966,777 US5316662A (en) | 1990-11-15 | 1992-10-27 | Integrated disengager stripper and its use in fluidized catalytic cracking process |
US07/966,776 US5314611A (en) | 1990-11-15 | 1992-10-27 | External integrated disengager stripper and its use in fluidized catalytic cracking process |
Publications (1)
Publication Number | Publication Date |
---|---|
ATE142247T1 true ATE142247T1 (en) | 1996-09-15 |
Family
ID=36791815
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
AT92309716T ATE142247T1 (en) | 1990-11-15 | 1992-10-23 | DRAIN EXTRACTION DEVICE CONTAINING DISSIPATION PLATES FOR FCC PROCESSES |
Country Status (8)
Country | Link |
---|---|
EP (1) | EP0593827B1 (en) |
CN (1) | CN1035773C (en) |
AT (1) | ATE142247T1 (en) |
AU (1) | AU649889B1 (en) |
CA (1) | CA2080974C (en) |
DE (1) | DE69213458T2 (en) |
ES (1) | ES2093798T3 (en) |
GR (1) | GR3021647T3 (en) |
Families Citing this family (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN1055492C (en) * | 1996-03-22 | 2000-08-16 | 中国石油化工集团公司 | Fast gas-solid separation and gas lead-out method and equipment for hoisting-pipe catalytic-cracking reaction system |
US5869008A (en) * | 1996-05-08 | 1999-02-09 | Shell Oil Company | Apparatus and method for the separation and stripping of fluid catalyst cracking particles from gaseous hydrocarbons |
FR2894842B1 (en) * | 2005-12-21 | 2008-02-01 | Inst Francais Du Petrole | NEW SOLID GAS SEPARATION AND STRIPING SYSTEM FOR FLUIDIZED BED CATALYTIC CRACKING UNITS |
US11261143B2 (en) * | 2019-04-12 | 2022-03-01 | Uop Llc | Apparatus and process for separating gases from catalyst |
Family Cites Families (13)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4500423A (en) * | 1981-02-26 | 1985-02-19 | Chevron Research Company | Separation of reacted hydrocarbons and catalyst in fluidized catalytic cracking |
US4414100A (en) * | 1981-12-29 | 1983-11-08 | Chevron Research Company | Fluidized catalytic cracking |
US4749471A (en) * | 1983-09-06 | 1988-06-07 | Mobil Oil Corporation | Closed FCC cyclone process |
CA1277276C (en) * | 1984-07-18 | 1990-12-04 | James H. Haddad | Fcc catalyst stripping method and apparatus |
US4927527A (en) * | 1984-07-18 | 1990-05-22 | Mobil Oil Corporation | Method for reducing overcracking during FCC catalyst separation |
US4572780A (en) * | 1984-10-22 | 1986-02-25 | Mobil Oil Corporation | Multistage stripper for FCC unit with catalyst separation by spinning |
CN1009659B (en) * | 1985-06-24 | 1990-09-19 | 法国石油公司 | Process and equipment for fluidized bed catalytic cracking |
US5043145A (en) * | 1986-08-21 | 1991-08-27 | Exxon Research & Engineering Company | Minimal holdup reactor grid |
GB8904409D0 (en) * | 1989-02-27 | 1989-04-12 | Shell Int Research | Process for the conversion of a hydrocarbonaceous feedstock |
US5062945A (en) * | 1988-09-23 | 1991-11-05 | Mobil Oil Corporation | Method of FCC spent catalyst stripping for improved efficiency and reduced hydrocarbon flow to regenerator |
US5059302A (en) * | 1989-05-16 | 1991-10-22 | Engelhard Corporation | Method and apparatus for the fluid catalytic cracking of hydrocarbon feed employing a separable mixture of catalyst and sorbent particles |
US4988430A (en) * | 1989-12-27 | 1991-01-29 | Uop | Supplying FCC lift gas directly from product vapors |
US5158669A (en) * | 1990-11-15 | 1992-10-27 | Uop | Disengager stripper |
-
1992
- 1992-10-20 CA CA002080974A patent/CA2080974C/en not_active Expired - Fee Related
- 1992-10-21 AU AU27278/92A patent/AU649889B1/en not_active Ceased
- 1992-10-23 EP EP92309716A patent/EP0593827B1/en not_active Expired - Lifetime
- 1992-10-23 AT AT92309716T patent/ATE142247T1/en not_active IP Right Cessation
- 1992-10-23 ES ES92309716T patent/ES2093798T3/en not_active Expired - Lifetime
- 1992-10-23 DE DE69213458T patent/DE69213458T2/en not_active Expired - Fee Related
- 1992-10-26 CN CN92112441A patent/CN1035773C/en not_active Expired - Fee Related
-
1996
- 1996-11-14 GR GR960403018T patent/GR3021647T3/en unknown
Also Published As
Publication number | Publication date |
---|---|
GR3021647T3 (en) | 1997-02-28 |
CN1086247A (en) | 1994-05-04 |
DE69213458D1 (en) | 1996-10-10 |
CN1035773C (en) | 1997-09-03 |
EP0593827A1 (en) | 1994-04-27 |
AU649889B1 (en) | 1994-06-02 |
EP0593827B1 (en) | 1996-09-04 |
DE69213458T2 (en) | 1997-01-02 |
CA2080974C (en) | 2004-02-17 |
CA2080974A1 (en) | 1994-04-21 |
ES2093798T3 (en) | 1997-01-01 |
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Legal Events
Date | Code | Title | Description |
---|---|---|---|
UEP | Publication of translation of european patent specification | ||
REN | Ceased due to non-payment of the annual fee |