JPS6132044B2 - - Google Patents
Info
- Publication number
- JPS6132044B2 JPS6132044B2 JP60124070A JP12407085A JPS6132044B2 JP S6132044 B2 JPS6132044 B2 JP S6132044B2 JP 60124070 A JP60124070 A JP 60124070A JP 12407085 A JP12407085 A JP 12407085A JP S6132044 B2 JPS6132044 B2 JP S6132044B2
- Authority
- JP
- Japan
- Prior art keywords
- riser
- chamber
- separation
- cone
- shroud
- Prior art date
- Legal status (The legal status 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 status listed.)
- Expired
Links
- 238000000926 separation method Methods 0.000 claims abstract description 28
- 239000007787 solid Substances 0.000 claims abstract description 26
- 239000003054 catalyst Substances 0.000 claims description 25
- 239000002245 particle Substances 0.000 claims description 15
- 238000005336 cracking Methods 0.000 claims description 13
- 229930195733 hydrocarbon Natural products 0.000 claims description 11
- 150000002430 hydrocarbons Chemical class 0.000 claims description 11
- 239000004215 Carbon black (E152) Substances 0.000 claims description 7
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 4
- 238000009835 boiling Methods 0.000 claims description 4
- 229910052799 carbon Inorganic materials 0.000 claims description 4
- 239000000295 fuel oil Substances 0.000 claims description 4
- 239000000446 fuel Substances 0.000 claims description 3
- 238000004231 fluid catalytic cracking Methods 0.000 claims description 2
- 150000002902 organometallic compounds Chemical class 0.000 claims description 2
- 239000000725 suspension Substances 0.000 abstract description 2
- 239000000463 material Substances 0.000 description 7
- 239000003921 oil Substances 0.000 description 5
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 4
- 239000007789 gas Substances 0.000 description 4
- 239000000047 product Substances 0.000 description 4
- 238000006243 chemical reaction Methods 0.000 description 3
- 238000011084 recovery Methods 0.000 description 3
- 230000008929 regeneration Effects 0.000 description 3
- 238000011069 regeneration method Methods 0.000 description 3
- MCMNRKCIXSYSNV-UHFFFAOYSA-N Zirconium dioxide Chemical compound O=[Zr]=O MCMNRKCIXSYSNV-UHFFFAOYSA-N 0.000 description 2
- 230000003197 catalytic effect Effects 0.000 description 2
- 239000004927 clay Substances 0.000 description 2
- 239000010779 crude oil Substances 0.000 description 2
- 239000012530 fluid Substances 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 239000002808 molecular sieve Substances 0.000 description 2
- 239000011236 particulate material Substances 0.000 description 2
- 239000000377 silicon dioxide Substances 0.000 description 2
- URGAHOPLAPQHLN-UHFFFAOYSA-N sodium aluminosilicate Chemical compound [Na+].[Al+3].[O-][Si]([O-])=O.[O-][Si]([O-])=O URGAHOPLAPQHLN-UHFFFAOYSA-N 0.000 description 2
- 229910000975 Carbon steel Inorganic materials 0.000 description 1
- 229910021536 Zeolite Inorganic materials 0.000 description 1
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 description 1
- 239000010962 carbon steel Substances 0.000 description 1
- 239000007795 chemical reaction product Substances 0.000 description 1
- 239000000571 coke Substances 0.000 description 1
- 230000000052 comparative effect Effects 0.000 description 1
- HNPSIPDUKPIQMN-UHFFFAOYSA-N dioxosilane;oxo(oxoalumanyloxy)alumane Chemical compound O=[Si]=O.O=[Al]O[Al]=O HNPSIPDUKPIQMN-UHFFFAOYSA-N 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000002474 experimental method Methods 0.000 description 1
- 238000005243 fluidization Methods 0.000 description 1
- 239000011159 matrix material Substances 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 150000002739 metals Chemical class 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000005504 petroleum refining Methods 0.000 description 1
- JTJMJGYZQZDUJJ-UHFFFAOYSA-N phencyclidine Chemical class C1CCCCN1C1(C=2C=CC=CC=2)CCCCC1 JTJMJGYZQZDUJJ-UHFFFAOYSA-N 0.000 description 1
- 239000011541 reaction mixture Substances 0.000 description 1
- 230000000630 rising effect Effects 0.000 description 1
- 239000002904 solvent Substances 0.000 description 1
- 239000010935 stainless steel Substances 0.000 description 1
- 229910001220 stainless steel Inorganic materials 0.000 description 1
- 238000005292 vacuum distillation Methods 0.000 description 1
- 239000010457 zeolite Substances 0.000 description 1
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
-
- 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
- B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
- B01J8/005—Separating solid material from the gas/liquid stream
- B01J8/0055—Separating solid material from the gas/liquid stream using cyclones
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Organic Chemistry (AREA)
- Engineering & Computer Science (AREA)
- General Chemical & Material Sciences (AREA)
- Separating Particles In Gases By Inertia (AREA)
- Cyclones (AREA)
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
- Separation Of Gases By Adsorption (AREA)
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US618641 | 1984-06-08 | ||
| US06/618,641 US4869880A (en) | 1984-06-08 | 1984-06-08 | Apparatus for the separation of solid particulates from a gaseous effluent |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS614518A JPS614518A (ja) | 1986-01-10 |
| JPS6132044B2 true JPS6132044B2 (Direct) | 1986-07-24 |
Family
ID=24478519
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP60124070A Granted JPS614518A (ja) | 1984-06-08 | 1985-06-07 | ガス状流出物から固体粒状物を分離する装置 |
Country Status (7)
| Country | Link |
|---|---|
| US (1) | US4869880A (Direct) |
| EP (1) | EP0167752B1 (Direct) |
| JP (1) | JPS614518A (Direct) |
| AT (1) | ATE48152T1 (Direct) |
| AU (1) | AU573831B2 (Direct) |
| CA (1) | CA1269624A (Direct) |
| DE (1) | DE3574394D1 (Direct) |
Families Citing this family (12)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US5182085A (en) * | 1990-05-17 | 1993-01-26 | Uop | Vented riser apparatus and method |
| US5190650A (en) * | 1991-06-24 | 1993-03-02 | Exxon Research And Engineering Company | Tangential solids separation transfer tunnel |
| US5290430A (en) * | 1991-11-13 | 1994-03-01 | Uop | Riser disengager with suspended catalyst separation zone |
| US5614083A (en) * | 1991-11-13 | 1997-03-25 | Uop | Riser disengager with suspended catalyst separation zone |
| US5393415A (en) * | 1991-12-06 | 1995-02-28 | Uop | FCC process with enclosed vented riser |
| US5723040A (en) * | 1994-09-22 | 1998-03-03 | Stone & Webster Engineering Corporation | Fluid catalytic cracking process and apparatus |
| US5662868A (en) * | 1994-09-22 | 1997-09-02 | Stone & Webster Engineering Corporation | Short residence time cracking apparatus and process |
| US5518695A (en) * | 1994-11-10 | 1996-05-21 | Uop | Vented riser with compact multiple cyclone arrangement |
| US5593643A (en) * | 1994-12-28 | 1997-01-14 | Uop | FCC arrangement with externally suspended catalyst separation zone |
| US6532835B1 (en) * | 1997-12-12 | 2003-03-18 | Research International, Inc. | High efficiency wetted surface cyclonic air sampler |
| BG107434A (bg) * | 2003-01-03 | 2003-08-29 | "Ресурс Плюс" Еоод | Разпръскващо устройство |
| US8349170B2 (en) * | 2008-05-14 | 2013-01-08 | Exxonmobil Research And Engineering Company | FCC reactor and riser design for short contact-time catalytic cracking of hydrocarbons |
Family Cites Families (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3312342A (en) * | 1964-03-27 | 1967-04-04 | Du Pont | Process and apparatus for impacting and elutriating solid particles |
| US4035284A (en) * | 1973-07-18 | 1977-07-12 | Mobil Oil Corporation | Method and system for regenerating fluidizable catalyst particles |
| AT364745B (de) * | 1975-03-24 | 1981-11-10 | Ashland Oil Inc | Verfahren und vorrichtung zum abscheiden feiner feststoffteilchen aus stroemenden gasen |
| US4390503A (en) * | 1981-05-13 | 1983-06-28 | Ashland Oil, Inc. | Carbometallic oil conversion with ballistic separation |
| US4394349A (en) * | 1981-07-06 | 1983-07-19 | Standard Oil Company (Indiana) | Apparatus for the fluidized catalytic cracking of hydrocarbon feedstock |
| US4405444A (en) * | 1982-11-08 | 1983-09-20 | Ashland Oil, Inc. | Method and means for charging foamed residual oils in contact with fluid solid particulate material |
| US4792437A (en) * | 1984-06-08 | 1988-12-20 | Ashland Oil, Inc. | Apparatus for the separation of solid particulates from a gaseous effluent |
-
1984
- 1984-06-08 US US06/618,641 patent/US4869880A/en not_active Expired - Fee Related
-
1985
- 1985-05-13 EP EP85105861A patent/EP0167752B1/en not_active Expired
- 1985-05-13 AT AT85105861T patent/ATE48152T1/de not_active IP Right Cessation
- 1985-05-13 DE DE8585105861T patent/DE3574394D1/de not_active Expired
- 1985-05-17 AU AU42618/85A patent/AU573831B2/en not_active Ceased
- 1985-05-21 CA CA000481976A patent/CA1269624A/en not_active Expired - Lifetime
- 1985-06-07 JP JP60124070A patent/JPS614518A/ja active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| EP0167752A1 (en) | 1986-01-15 |
| ATE48152T1 (de) | 1989-12-15 |
| DE3574394D1 (en) | 1989-12-28 |
| AU573831B2 (en) | 1988-06-23 |
| JPS614518A (ja) | 1986-01-10 |
| EP0167752B1 (en) | 1989-11-23 |
| CA1269624A (en) | 1990-05-29 |
| US4869880A (en) | 1989-09-26 |
| AU4261885A (en) | 1985-12-12 |
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