NO337658B1 - Fremgangsmåte for fluid katalytisk krakking av hydrokarboner. - Google Patents
Fremgangsmåte for fluid katalytisk krakking av hydrokarboner. Download PDFInfo
- Publication number
- NO337658B1 NO337658B1 NO20063753A NO20063753A NO337658B1 NO 337658 B1 NO337658 B1 NO 337658B1 NO 20063753 A NO20063753 A NO 20063753A NO 20063753 A NO20063753 A NO 20063753A NO 337658 B1 NO337658 B1 NO 337658B1
- Authority
- NO
- Norway
- Prior art keywords
- catalyst
- cyclone
- reaction zone
- catalyst particles
- hydrocarbons
- Prior art date
Links
- 150000002430 hydrocarbons Chemical class 0.000 title claims description 37
- 229930195733 hydrocarbon Natural products 0.000 title claims description 35
- 238000000034 method Methods 0.000 title claims description 25
- 238000004231 fluid catalytic cracking Methods 0.000 title claims description 6
- 239000003054 catalyst Substances 0.000 claims description 86
- 238000006243 chemical reaction Methods 0.000 claims description 47
- 150000001336 alkenes Chemical class 0.000 claims description 37
- 239000002245 particle Substances 0.000 claims description 29
- 238000000926 separation method Methods 0.000 claims description 23
- 239000004215 Carbon black (E152) Substances 0.000 claims description 15
- 230000008929 regeneration Effects 0.000 claims description 13
- 238000011069 regeneration method Methods 0.000 claims description 13
- 239000010457 zeolite Substances 0.000 claims description 9
- 229910021536 Zeolite Inorganic materials 0.000 claims description 6
- HNPSIPDUKPIQMN-UHFFFAOYSA-N dioxosilane;oxo(oxoalumanyloxy)alumane Chemical compound O=[Si]=O.O=[Al]O[Al]=O HNPSIPDUKPIQMN-UHFFFAOYSA-N 0.000 claims description 6
- 238000009835 boiling Methods 0.000 claims description 5
- 125000004432 carbon atom Chemical group C* 0.000 claims description 5
- 238000005235 decoking Methods 0.000 claims description 5
- 238000011144 upstream manufacturing Methods 0.000 claims description 5
- 239000012530 fluid Substances 0.000 claims description 4
- 239000007795 chemical reaction product Substances 0.000 claims description 3
- 238000002347 injection Methods 0.000 claims description 3
- 239000007924 injection Substances 0.000 claims description 3
- 239000003208 petroleum Substances 0.000 claims description 3
- 238000004523 catalytic cracking Methods 0.000 claims description 2
- 238000004508 fractional distillation Methods 0.000 claims description 2
- 239000000463 material Substances 0.000 claims description 2
- 239000011541 reaction mixture Substances 0.000 claims description 2
- 229930195734 saturated hydrocarbon Natural products 0.000 claims description 2
- 230000001590 oxidative effect Effects 0.000 claims 1
- 239000007789 gas Substances 0.000 description 13
- 238000005336 cracking Methods 0.000 description 11
- 230000000694 effects Effects 0.000 description 8
- 238000004519 manufacturing process Methods 0.000 description 8
- 239000000047 product Substances 0.000 description 8
- 239000000571 coke Substances 0.000 description 7
- 239000007787 solid Substances 0.000 description 5
- 238000005194 fractionation Methods 0.000 description 4
- 239000000203 mixture Substances 0.000 description 4
- JTJMJGYZQZDUJJ-UHFFFAOYSA-N phencyclidine Chemical class C1CCCCN1C1(C=2C=CC=CC=2)CCCCC1 JTJMJGYZQZDUJJ-UHFFFAOYSA-N 0.000 description 4
- 238000011027 product recovery Methods 0.000 description 4
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 3
- 239000001301 oxygen Substances 0.000 description 3
- 229910052760 oxygen Inorganic materials 0.000 description 3
- 239000011148 porous material Substances 0.000 description 3
- QQONPFPTGQHPMA-UHFFFAOYSA-N propylene Natural products CC=C QQONPFPTGQHPMA-UHFFFAOYSA-N 0.000 description 3
- 125000004805 propylene group Chemical group [H]C([H])([H])C([H])([*:1])C([H])([H])[*:2] 0.000 description 3
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 2
- 150000001875 compounds Chemical class 0.000 description 2
- 150000001925 cycloalkenes Chemical class 0.000 description 2
- 238000006356 dehydrogenation reaction Methods 0.000 description 2
- JRZJOMJEPLMPRA-UHFFFAOYSA-N olefin Natural products CCCCCCCC=C JRZJOMJEPLMPRA-UHFFFAOYSA-N 0.000 description 2
- 239000012071 phase Substances 0.000 description 2
- 238000010517 secondary reaction Methods 0.000 description 2
- 239000012808 vapor phase Substances 0.000 description 2
- 239000000654 additive Substances 0.000 description 1
- 230000000996 additive effect Effects 0.000 description 1
- 230000029936 alkylation Effects 0.000 description 1
- 238000005804 alkylation reaction Methods 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
- 229910000323 aluminium silicate Inorganic materials 0.000 description 1
- 125000006615 aromatic heterocyclic group Chemical group 0.000 description 1
- 230000000903 blocking effect Effects 0.000 description 1
- 239000006227 byproduct Substances 0.000 description 1
- 239000003575 carbonaceous material Substances 0.000 description 1
- 230000003197 catalytic effect Effects 0.000 description 1
- 239000000567 combustion gas Substances 0.000 description 1
- 238000002485 combustion reaction Methods 0.000 description 1
- 230000009849 deactivation Effects 0.000 description 1
- 239000003085 diluting agent Substances 0.000 description 1
- 238000009826 distribution Methods 0.000 description 1
- 230000009977 dual effect Effects 0.000 description 1
- 230000003628 erosive effect Effects 0.000 description 1
- 239000000446 fuel Substances 0.000 description 1
- 239000001257 hydrogen Substances 0.000 description 1
- 229910052739 hydrogen Inorganic materials 0.000 description 1
- 125000004435 hydrogen atom Chemical class [H]* 0.000 description 1
- 229910052809 inorganic oxide Inorganic materials 0.000 description 1
- 238000006317 isomerization reaction Methods 0.000 description 1
- 239000003350 kerosene Substances 0.000 description 1
- 125000003367 polycyclic group Chemical group 0.000 description 1
- 230000035484 reaction time Effects 0.000 description 1
- 238000011084 recovery Methods 0.000 description 1
- 238000007363 ring formation reaction Methods 0.000 description 1
- 238000007086 side reaction Methods 0.000 description 1
- 239000000377 silicon dioxide Substances 0.000 description 1
- 125000000383 tetramethylene group Chemical group [H]C([H])([*:1])C([H])([H])C([H])([H])C([H])([H])[*:2] 0.000 description 1
- 238000010518 undesired secondary reaction Methods 0.000 description 1
- 238000009827 uniform distribution Methods 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
-
- 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
Landscapes
- Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
- Catalysts (AREA)
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US53890604P | 2004-01-23 | 2004-01-23 | |
| PCT/US2005/001724 WO2005073347A1 (en) | 2004-01-23 | 2005-01-19 | System and method for selective component cracking to maximize production of light olefins |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| NO20063753L NO20063753L (no) | 2006-08-22 |
| NO337658B1 true NO337658B1 (no) | 2016-05-30 |
Family
ID=34826026
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| NO20063753A NO337658B1 (no) | 2004-01-23 | 2006-08-22 | Fremgangsmåte for fluid katalytisk krakking av hydrokarboner. |
Country Status (12)
| Country | Link |
|---|---|
| US (1) | US20050161369A1 (ko) |
| EP (1) | EP1713884B1 (ko) |
| JP (1) | JP2007518866A (ko) |
| KR (1) | KR100985288B1 (ko) |
| CN (1) | CN1910264A (ko) |
| AU (1) | AU2005207859B2 (ko) |
| BR (1) | BRPI0506971B1 (ko) |
| CA (1) | CA2553783C (ko) |
| MX (1) | MXPA06008184A (ko) |
| NO (1) | NO337658B1 (ko) |
| WO (1) | WO2005073347A1 (ko) |
| ZA (1) | ZA200606044B (ko) |
Families Citing this family (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| KR101503069B1 (ko) * | 2008-10-17 | 2015-03-17 | 에스케이이노베이션 주식회사 | 유동층 접촉 분해 공정의 경질 사이클 오일로부터 고부가 방향족 및 올레핀을 제조하는 방법 |
| US8137631B2 (en) * | 2008-12-11 | 2012-03-20 | Uop Llc | Unit, system and process for catalytic cracking |
| US9452404B2 (en) * | 2012-07-12 | 2016-09-27 | Lummus Technology Inc. | Fluid cracking process and apparatus for maximizing light olefins or middle distillates and light olefins |
| RU2728777C1 (ru) | 2016-09-16 | 2020-07-31 | ЛАММУС ТЕКНОЛОДЖИ ЭлЭлСи | Способ каталитического крекинга со взвешенным катализатором и устройство для максимизации выхода легкого олефина и других приложений |
| FR3090684B1 (fr) * | 2018-12-19 | 2021-08-27 | Ifp Energies Now | Conversion d’un brut pétrolier en lit fluidisé, avec zones de différents temps de contact |
| US20220275288A1 (en) * | 2019-08-05 | 2022-09-01 | Sabic Global Technologies B.V. | Multiple dense phase risers to maximize light olefins yields for naphtha catalytic cracking |
| CN111408323A (zh) * | 2020-04-17 | 2020-07-14 | 董国亮 | 一种降低催化剂管道应力以及衬里磨损的反应再生装置 |
Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4422925A (en) * | 1981-12-28 | 1983-12-27 | Texaco Inc. | Catalytic cracking |
| US4749471A (en) * | 1983-09-06 | 1988-06-07 | Mobil Oil Corporation | Closed FCC cyclone process |
| US5248411A (en) * | 1990-11-30 | 1993-09-28 | Texaco Inc. | Apparatus and process for withdrawing stripper gas from an FCC reactor vessel |
| EP0654518B1 (en) * | 1993-11-22 | 1998-12-16 | Abb Lummus Global Inc. | Control method for fluid catalytic cracking coupled riser cyclone |
Family Cites Families (15)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4588558A (en) * | 1983-09-06 | 1986-05-13 | Mobil Oil Corporation | Closed FCC cyclone system |
| US4623446A (en) * | 1984-05-21 | 1986-11-18 | Mobil Oil Corporation | Closed cyclone FCC catalyst separation with stripping gas injection and direct steam injection |
| US5264115A (en) * | 1987-12-30 | 1993-11-23 | Compagnie De Raffinage Et De Distribution Total France | Process and apparatus for fluidized bed hydrocarbon conversion |
| US5271826A (en) * | 1988-03-03 | 1993-12-21 | Mobil Oil Corporation | Catalytic cracking of coke producing hydrocarbons |
| US5234578A (en) * | 1988-08-26 | 1993-08-10 | Uop | Fluidized catalytic cracking process utilizing a high temperature reactor |
| US4968406A (en) * | 1988-10-29 | 1990-11-06 | Mobil Oil Corporation | Increasing feed volume throughput in FCC process |
| CA1327177C (en) * | 1988-11-18 | 1994-02-22 | Alan R. Goelzer | Process for selectively maximizing product production in fluidized catalytic cracking of hydrocarbons |
| US5279727A (en) * | 1991-12-27 | 1994-01-18 | Amoco Corporation | Open-bottomed cyclone with solids separation tube and method |
| US6118035A (en) * | 1998-05-05 | 2000-09-12 | Exxon Research And Engineering Co. | Process for selectively producing light olefins in a fluid catalytic cracking process from a naphtha/steam feed |
| US6106697A (en) | 1998-05-05 | 2000-08-22 | Exxon Research And Engineering Company | Two stage fluid catalytic cracking process for selectively producing b. C.su2 to C4 olefins |
| US6313366B1 (en) * | 1998-05-05 | 2001-11-06 | Exxonmobile Chemical Patents, Inc. | Process for selectively producing C3 olefins in a fluid catalytic cracking process |
| US5944982A (en) * | 1998-10-05 | 1999-08-31 | Uop Llc | Method for high severity cracking |
| US6760394B1 (en) * | 1999-08-11 | 2004-07-06 | Broadcom Corporation | CMOS lock detect with double protection |
| US6538169B1 (en) * | 2000-11-13 | 2003-03-25 | Uop Llc | FCC process with improved yield of light olefins |
| US6709572B2 (en) * | 2002-03-05 | 2004-03-23 | Exxonmobil Research And Engineering Company | Catalytic cracking process |
-
2005
- 2005-01-18 US US11/039,125 patent/US20050161369A1/en not_active Abandoned
- 2005-01-19 AU AU2005207859A patent/AU2005207859B2/en active Active
- 2005-01-19 JP JP2006551243A patent/JP2007518866A/ja active Pending
- 2005-01-19 KR KR1020067014571A patent/KR100985288B1/ko active IP Right Grant
- 2005-01-19 CA CA2553783A patent/CA2553783C/en active Active
- 2005-01-19 EP EP05705923.0A patent/EP1713884B1/en active Active
- 2005-01-19 BR BRPI0506971-8A patent/BRPI0506971B1/pt not_active IP Right Cessation
- 2005-01-19 CN CNA2005800030167A patent/CN1910264A/zh active Pending
- 2005-01-19 WO PCT/US2005/001724 patent/WO2005073347A1/en not_active Application Discontinuation
- 2005-01-19 MX MXPA06008184A patent/MXPA06008184A/es active IP Right Grant
-
2006
- 2006-07-21 ZA ZA200606044A patent/ZA200606044B/xx unknown
- 2006-08-22 NO NO20063753A patent/NO337658B1/no not_active IP Right Cessation
Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4422925A (en) * | 1981-12-28 | 1983-12-27 | Texaco Inc. | Catalytic cracking |
| US4749471A (en) * | 1983-09-06 | 1988-06-07 | Mobil Oil Corporation | Closed FCC cyclone process |
| US5248411A (en) * | 1990-11-30 | 1993-09-28 | Texaco Inc. | Apparatus and process for withdrawing stripper gas from an FCC reactor vessel |
| EP0654518B1 (en) * | 1993-11-22 | 1998-12-16 | Abb Lummus Global Inc. | Control method for fluid catalytic cracking coupled riser cyclone |
Also Published As
| Publication number | Publication date |
|---|---|
| KR100985288B1 (ko) | 2010-10-04 |
| AU2005207859B2 (en) | 2010-01-07 |
| US20050161369A1 (en) | 2005-07-28 |
| CA2553783C (en) | 2013-03-26 |
| JP2007518866A (ja) | 2007-07-12 |
| NO20063753L (no) | 2006-08-22 |
| EP1713884B1 (en) | 2018-09-26 |
| KR20070018836A (ko) | 2007-02-14 |
| ZA200606044B (en) | 2007-12-27 |
| CN1910264A (zh) | 2007-02-07 |
| WO2005073347A1 (en) | 2005-08-11 |
| CA2553783A1 (en) | 2005-08-11 |
| BRPI0506971A (pt) | 2007-07-03 |
| MXPA06008184A (es) | 2007-01-26 |
| BRPI0506971B1 (pt) | 2020-12-08 |
| EP1713884A1 (en) | 2006-10-25 |
| AU2005207859A1 (en) | 2005-08-11 |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| MM1K | Lapsed by not paying the annual fees |