JPH0247517B2 - - Google Patents
Info
- Publication number
- JPH0247517B2 JPH0247517B2 JP58150100A JP15010083A JPH0247517B2 JP H0247517 B2 JPH0247517 B2 JP H0247517B2 JP 58150100 A JP58150100 A JP 58150100A JP 15010083 A JP15010083 A JP 15010083A JP H0247517 B2 JPH0247517 B2 JP H0247517B2
- Authority
- JP
- Japan
- Prior art keywords
- riser
- catalyst
- oil
- zone
- hydrocarbon
- 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 - Lifetime
Links
- 239000003921 oil Substances 0.000 claims description 88
- 239000003054 catalyst Substances 0.000 claims description 78
- 238000000034 method Methods 0.000 claims description 50
- 229930195733 hydrocarbon Natural products 0.000 claims description 34
- 150000002430 hydrocarbons Chemical class 0.000 claims description 34
- 238000009835 boiling Methods 0.000 claims description 31
- 239000010779 crude oil Substances 0.000 claims description 31
- 239000002245 particle Substances 0.000 claims description 27
- 230000008569 process Effects 0.000 claims description 24
- 239000004215 Carbon black (E152) Substances 0.000 claims description 22
- 239000007789 gas Substances 0.000 claims description 21
- 238000006243 chemical reaction Methods 0.000 claims description 17
- 239000000725 suspension Substances 0.000 claims description 17
- 239000003502 gasoline Substances 0.000 claims description 13
- 238000000926 separation method Methods 0.000 claims description 12
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 10
- 239000012535 impurity Substances 0.000 claims description 10
- 229910052799 carbon Inorganic materials 0.000 claims description 9
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 9
- 229910021536 Zeolite Inorganic materials 0.000 claims description 7
- HNPSIPDUKPIQMN-UHFFFAOYSA-N dioxosilane;oxo(oxoalumanyloxy)alumane Chemical compound O=[Si]=O.O=[Al]O[Al]=O HNPSIPDUKPIQMN-UHFFFAOYSA-N 0.000 claims description 7
- 239000010457 zeolite Substances 0.000 claims description 7
- 238000011084 recovery Methods 0.000 claims description 5
- 230000007704 transition Effects 0.000 claims description 5
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 claims description 4
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 claims description 4
- 238000004519 manufacturing process Methods 0.000 claims description 4
- 229910052717 sulfur Inorganic materials 0.000 claims description 4
- 239000011593 sulfur Substances 0.000 claims description 4
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 claims description 3
- 239000001257 hydrogen Substances 0.000 claims description 3
- 229910052739 hydrogen Inorganic materials 0.000 claims description 3
- 238000011068 loading method Methods 0.000 claims description 3
- 229910052757 nitrogen Inorganic materials 0.000 claims description 2
- 150000002902 organometallic compounds Chemical class 0.000 claims description 2
- 230000000149 penetrating effect Effects 0.000 claims description 2
- 238000007670 refining Methods 0.000 claims description 2
- 230000001804 emulsifying effect Effects 0.000 claims 1
- 229910052751 metal Inorganic materials 0.000 description 20
- 239000002184 metal Substances 0.000 description 20
- 238000004231 fluid catalytic cracking Methods 0.000 description 17
- PXHVJJICTQNCMI-UHFFFAOYSA-N Nickel Chemical compound [Ni] PXHVJJICTQNCMI-UHFFFAOYSA-N 0.000 description 16
- 229910001385 heavy metal Inorganic materials 0.000 description 16
- 239000000047 product Substances 0.000 description 16
- 238000005336 cracking Methods 0.000 description 15
- 239000000571 coke Substances 0.000 description 14
- 239000000463 material Substances 0.000 description 13
- 239000002243 precursor Substances 0.000 description 10
- 230000003197 catalytic effect Effects 0.000 description 8
- 239000007788 liquid Substances 0.000 description 8
- 239000000126 substance Substances 0.000 description 8
- 229910052759 nickel Inorganic materials 0.000 description 7
- 239000000446 fuel Substances 0.000 description 6
- 150000002739 metals Chemical class 0.000 description 6
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 5
- 230000015572 biosynthetic process Effects 0.000 description 5
- 238000004821 distillation Methods 0.000 description 5
- 230000000694 effects Effects 0.000 description 5
- 238000012545 processing Methods 0.000 description 5
- 229910052720 vanadium Inorganic materials 0.000 description 5
- LEONUFNNVUYDNQ-UHFFFAOYSA-N vanadium atom Chemical compound [V] LEONUFNNVUYDNQ-UHFFFAOYSA-N 0.000 description 5
- 239000000203 mixture Substances 0.000 description 4
- 238000009825 accumulation Methods 0.000 description 3
- 150000001875 compounds Chemical class 0.000 description 3
- 239000010949 copper Substances 0.000 description 3
- 238000010586 diagram Methods 0.000 description 3
- 239000000295 fuel oil Substances 0.000 description 3
- 238000012986 modification Methods 0.000 description 3
- 230000004048 modification Effects 0.000 description 3
- 230000000607 poisoning effect Effects 0.000 description 3
- 238000012360 testing method Methods 0.000 description 3
- 238000004227 thermal cracking Methods 0.000 description 3
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 2
- DGAQECJNVWCQMB-PUAWFVPOSA-M Ilexoside XXIX Chemical compound C[C@@H]1CC[C@@]2(CC[C@@]3(C(=CC[C@H]4[C@]3(CC[C@@H]5[C@@]4(CC[C@@H](C5(C)C)OS(=O)(=O)[O-])C)C)[C@@H]2[C@]1(C)O)C)C(=O)O[C@H]6[C@@H]([C@H]([C@@H]([C@H](O6)CO)O)O)O.[Na+] DGAQECJNVWCQMB-PUAWFVPOSA-M 0.000 description 2
- 238000007792 addition Methods 0.000 description 2
- 230000002411 adverse Effects 0.000 description 2
- 125000003118 aryl group Chemical group 0.000 description 2
- 238000004523 catalytic cracking Methods 0.000 description 2
- 238000001833 catalytic reforming Methods 0.000 description 2
- 238000009833 condensation Methods 0.000 description 2
- 230000005494 condensation Effects 0.000 description 2
- 238000007796 conventional method Methods 0.000 description 2
- 229910052802 copper Inorganic materials 0.000 description 2
- 238000006356 dehydrogenation reaction Methods 0.000 description 2
- 238000013461 design Methods 0.000 description 2
- 239000012013 faujasite Substances 0.000 description 2
- 230000009969 flowable effect Effects 0.000 description 2
- 239000008187 granular material Substances 0.000 description 2
- 230000002452 interceptive effect Effects 0.000 description 2
- 229910052742 iron Inorganic materials 0.000 description 2
- 239000011159 matrix material Substances 0.000 description 2
- 229910017464 nitrogen compound Inorganic materials 0.000 description 2
- 150000002830 nitrogen compounds Chemical class 0.000 description 2
- 239000003208 petroleum Substances 0.000 description 2
- 239000002574 poison Substances 0.000 description 2
- 231100000614 poison Toxicity 0.000 description 2
- 239000011148 porous material Substances 0.000 description 2
- 229910052761 rare earth metal Inorganic materials 0.000 description 2
- 150000002910 rare earth metals Chemical group 0.000 description 2
- 239000000376 reactant Substances 0.000 description 2
- 230000008929 regeneration Effects 0.000 description 2
- 238000011069 regeneration method Methods 0.000 description 2
- 229910052708 sodium Inorganic materials 0.000 description 2
- 239000011734 sodium Substances 0.000 description 2
- 239000007787 solid Substances 0.000 description 2
- 238000005979 thermal decomposition reaction Methods 0.000 description 2
- -1 C 5 hydrocarbons Chemical class 0.000 description 1
- CWYNVVGOOAEACU-UHFFFAOYSA-N Fe2+ Chemical compound [Fe+2] CWYNVVGOOAEACU-UHFFFAOYSA-N 0.000 description 1
- 238000005727 Friedel-Crafts reaction Methods 0.000 description 1
- ZLMJMSJWJFRBEC-UHFFFAOYSA-N Potassium Chemical compound [K] ZLMJMSJWJFRBEC-UHFFFAOYSA-N 0.000 description 1
- YKTSYUJCYHOUJP-UHFFFAOYSA-N [O--].[Al+3].[Al+3].[O-][Si]([O-])([O-])[O-] Chemical compound [O--].[Al+3].[Al+3].[O-][Si]([O-])([O-])[O-] YKTSYUJCYHOUJP-UHFFFAOYSA-N 0.000 description 1
- 238000005299 abrasion Methods 0.000 description 1
- 230000002378 acidificating effect Effects 0.000 description 1
- 239000000654 additive Substances 0.000 description 1
- 230000000996 additive effect Effects 0.000 description 1
- 238000013459 approach Methods 0.000 description 1
- 239000010426 asphalt Substances 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 238000003421 catalytic decomposition reaction Methods 0.000 description 1
- 238000004517 catalytic hydrocracking Methods 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 238000004939 coking Methods 0.000 description 1
- 238000002485 combustion reaction Methods 0.000 description 1
- 238000010668 complexation reaction Methods 0.000 description 1
- 239000000470 constituent Substances 0.000 description 1
- 239000000356 contaminant Substances 0.000 description 1
- 238000011109 contamination Methods 0.000 description 1
- 239000012084 conversion product Substances 0.000 description 1
- 238000012962 cracking technique Methods 0.000 description 1
- 238000010908 decantation Methods 0.000 description 1
- 238000010612 desalination reaction Methods 0.000 description 1
- 238000009826 distribution Methods 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 238000001704 evaporation Methods 0.000 description 1
- 230000008020 evaporation Effects 0.000 description 1
- 239000010419 fine particle Substances 0.000 description 1
- 230000004907 flux Effects 0.000 description 1
- 239000010763 heavy fuel oil Substances 0.000 description 1
- 230000008018 melting Effects 0.000 description 1
- 238000002844 melting Methods 0.000 description 1
- 239000007769 metal material Substances 0.000 description 1
- 239000010747 number 6 fuel oil Substances 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 238000002161 passivation Methods 0.000 description 1
- 239000008188 pellet Substances 0.000 description 1
- 230000000737 periodic effect Effects 0.000 description 1
- 229910052700 potassium Inorganic materials 0.000 description 1
- 239000011591 potassium Substances 0.000 description 1
- 239000010453 quartz Substances 0.000 description 1
- 230000009467 reduction Effects 0.000 description 1
- 238000011160 research Methods 0.000 description 1
- 239000003079 shale oil Substances 0.000 description 1
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N silicon dioxide Inorganic materials O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 1
- 238000000638 solvent extraction Methods 0.000 description 1
- 238000009718 spray deposition Methods 0.000 description 1
- 150000003464 sulfur compounds Chemical class 0.000 description 1
- 238000010998 test method Methods 0.000 description 1
- 230000008719 thickening Effects 0.000 description 1
- 231100000331 toxic Toxicity 0.000 description 1
- 230000002588 toxic effect Effects 0.000 description 1
- 238000012546 transfer Methods 0.000 description 1
- 238000005292 vacuum distillation Methods 0.000 description 1
- 238000009834 vaporization Methods 0.000 description 1
- 230000008016 vaporization Effects 0.000 description 1
- 239000002699 waste material 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
- B01J8/08—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with moving particles
- B01J8/085—Feeding reactive fluids
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Engineering & Computer Science (AREA)
- General Chemical & Material Sciences (AREA)
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US411719 | 1982-08-19 | ||
| US06/411,719 US4435279A (en) | 1982-08-19 | 1982-08-19 | Method and apparatus for converting oil feeds |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS5953591A JPS5953591A (ja) | 1984-03-28 |
| JPH0247517B2 true JPH0247517B2 (en, 2012) | 1990-10-19 |
Family
ID=23630040
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP58150100A Granted JPS5953591A (ja) | 1982-08-19 | 1983-08-17 | 供給油の転化方法および装置 |
Country Status (4)
| Country | Link |
|---|---|
| US (1) | US4435279A (en, 2012) |
| EP (1) | EP0101553A3 (en, 2012) |
| JP (1) | JPS5953591A (en, 2012) |
| CA (1) | CA1205407A (en, 2012) |
Families Citing this family (50)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4495063A (en) * | 1981-05-13 | 1985-01-22 | Ashland Oil, Inc. | Carbometallic oil conversion with ballistic separation |
| US5045176A (en) * | 1981-05-13 | 1991-09-03 | Ashland Oil, Inc. | Carbometallic oil conversion with ballistic separation |
| US4894141A (en) * | 1981-09-01 | 1990-01-16 | Ashland Oil, Inc. | Combination process for upgrading residual oils |
| US4650566A (en) * | 1984-05-30 | 1987-03-17 | Mobil Oil Corporation | FCC reactor multi-feed nozzle system |
| US4541919A (en) * | 1984-08-07 | 1985-09-17 | Mobil Oil Corporation | Shape selective dewaxing using coke modified large pore zeolites |
| FR2584732B1 (fr) * | 1985-07-10 | 1988-08-19 | Raffinage Cie Francaise | Procede et dispositif pour le craquage catalytique de charges d'hydrocarbures, avec controle de la temperature de reaction |
| CN87100803A (zh) * | 1986-02-24 | 1987-10-07 | 恩格尔哈德公司 | 改进型烃转化方法 |
| US4802971A (en) * | 1986-09-03 | 1989-02-07 | Mobil Oil Corporation | Single riser fluidized catalytic cracking process utilizing hydrogen and carbon-hydrogen contributing fragments |
| AU605188B2 (en) * | 1986-09-03 | 1991-01-10 | Mobil Oil Corporation | Processing of activated heavy hydrocarbon feeds |
| JPS6384632A (ja) * | 1986-09-03 | 1988-04-15 | モービル・オイル・コーポレイション | 流動接触分解方法 |
| US4853105A (en) * | 1986-09-03 | 1989-08-01 | Mobil Oil Corporation | Multiple riser fluidized catalytic cracking process utilizing hydrogen and carbon-hydrogen contributing fragments |
| US4863585A (en) * | 1986-09-03 | 1989-09-05 | Mobil Oil Corporation | Fluidized catalytic cracking process utilizing a C3-C4 paraffin-rich Co-feed and mixed catalyst system with selective reactivation of the medium pore silicate zeolite component thereofo |
| US4826586A (en) * | 1986-09-03 | 1989-05-02 | Mobil Coil Corporation | Single riser fluidized catalytic cracking process utilizing a C3-4 paraffin-rich co-feed and mixed catalyst system |
| US4752375A (en) * | 1986-09-03 | 1988-06-21 | Mobil Oil Corporation | Single riser fluidized catalytic cracking process utilizing a C3-4 paraffin-rich co-feed and mixed catalyst system |
| US4717467A (en) * | 1987-05-15 | 1988-01-05 | Mobil Oil Corporation | Process for mixing fluid catalytic cracking hydrocarbon feed and catalyst |
| FR2628117B2 (fr) * | 1988-01-21 | 1992-10-16 | Inst Francais Du Petrole | Procede de craquage catalytique |
| US5087349A (en) * | 1988-11-18 | 1992-02-11 | Stone & Webster Engineering Corporation | Process for selectively maximizing product production in fluidized catalytic cracking of hydrocarbons |
| US5160706A (en) * | 1989-10-17 | 1992-11-03 | Shell Oil Company | Process for the catalytic cracking of a hydrocarbon oil |
| US5868923A (en) * | 1991-05-02 | 1999-02-09 | Texaco Inc | Hydroconversion process |
| US5314610A (en) * | 1992-05-29 | 1994-05-24 | Abb Lummus Crest Inc. | Staged catalytic cracking process |
| US5316657A (en) * | 1992-11-27 | 1994-05-31 | Uop | FCC process for de-gassing spent catalyst boundary layer |
| US6059957A (en) * | 1996-09-16 | 2000-05-09 | Texaco Inc. | Methods for adding value to heavy oil |
| US5935419A (en) * | 1996-09-16 | 1999-08-10 | Texaco Inc. | Methods for adding value to heavy oil utilizing a soluble metal catalyst |
| WO1999055801A1 (en) * | 1998-04-28 | 1999-11-04 | Exxon Research And Engineering Company | Fluid catalytic cracking process for converting a plurality of feeds |
| US6123832A (en) * | 1998-04-28 | 2000-09-26 | Exxon Research And Engineering Co. | Fluid catalytic cracking process for converting hydrocarbon mixtures |
| CN1078094C (zh) | 1999-04-23 | 2002-01-23 | 中国石油化工集团公司 | 一种用于流化催化转化的提升管反应器 |
| US20040104149A1 (en) * | 1999-08-20 | 2004-06-03 | Lomas David A. | Controllable volume reactor and process |
| US20010042702A1 (en) * | 2000-04-17 | 2001-11-22 | Stuntz Gordon F. | Cycle oil conversion process |
| US6569315B2 (en) | 2000-04-17 | 2003-05-27 | Exxonmobil Research And Engineering Company | Cycle oil conversion process |
| US20010042701A1 (en) | 2000-04-17 | 2001-11-22 | Stuntz Gordon F. | Cycle oil conversion process |
| US6569316B2 (en) | 2000-04-17 | 2003-05-27 | Exxonmobil Research And Engineering Company | Cycle oil conversion process incorporating shape-selective zeolite catalysts |
| US20010042700A1 (en) * | 2000-04-17 | 2001-11-22 | Swan, George A. | Naphtha and cycle oil conversion process |
| US6565739B2 (en) | 2000-04-17 | 2003-05-20 | Exxonmobil Research And Engineering Company | Two stage FCC process incorporating interstage hydroprocessing |
| ATE498670T1 (de) | 2003-07-04 | 2011-03-15 | Shell Int Research | Verfahren zur herstellung eines fischer-tropsch- produkts |
| US20070205139A1 (en) * | 2006-03-01 | 2007-09-06 | Sathit Kulprathipanja | Fcc dual elevation riser feed distributors for gasoline and light olefin modes of operation |
| US7901640B2 (en) * | 2008-05-13 | 2011-03-08 | Uop Llc | Optimized counter-current flow baffle |
| US7906081B2 (en) * | 2008-05-13 | 2011-03-15 | Uop Llc | Internal grids for adsorbent chambers and reactors |
| US7718146B2 (en) * | 2008-05-13 | 2010-05-18 | Uop Llc | Enhanced bed separation in a styrene monomer reactor using milled plates |
| CN102233253B (zh) * | 2010-05-06 | 2013-11-06 | 中国石油天然气股份有限公司 | 一种加工重油的提升管催化装置和应用 |
| US8927794B2 (en) | 2011-04-21 | 2015-01-06 | Shell Oil Company | Process for regenerating a coked catalytic cracking catalyst |
| AU2012245090A1 (en) * | 2011-04-21 | 2013-10-31 | Shell Internationale Research Maatschappij B.V. | Process for converting a solid biomass material |
| CN103597056A (zh) * | 2011-04-21 | 2014-02-19 | 国际壳牌研究有限公司 | 转化固体生物质材料的方法 |
| US20120271074A1 (en) * | 2011-04-21 | 2012-10-25 | Shell Oil Company | Process for converting a solid biomass material |
| CN103597055A (zh) * | 2011-04-21 | 2014-02-19 | 国际壳牌研究有限公司 | 转化固体生物质材料的方法 |
| US9006489B2 (en) * | 2011-06-07 | 2015-04-14 | Jiangsu Sinorgchem Technology Co., Ltd. | Method for pretreating and using copper-based catalyst |
| US9109177B2 (en) | 2011-12-12 | 2015-08-18 | Ensyn Renewables, Inc. | Systems and methods for renewable fuel |
| US8936758B2 (en) * | 2012-03-20 | 2015-01-20 | Uop Llc | Process and apparatus for mixing two streams of catalyst |
| EP2841536A1 (en) | 2012-04-23 | 2015-03-04 | Shell Internationale Research Maatschappij B.V. | Process for converting a solid biomass material |
| TWI645026B (zh) | 2013-06-26 | 2018-12-21 | 安信再生公司 | 可再生燃料之系統及方法 |
| US20220370975A1 (en) * | 2021-05-18 | 2022-11-24 | Uop Llc | Apparatus for distributing feed with a cluster of orifices on a side of the distributor |
Family Cites Families (14)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3406112A (en) | 1967-12-26 | 1968-10-15 | Mobil Oil Corp | Catalytic cracking process |
| US3617497A (en) | 1969-06-25 | 1971-11-02 | Gulf Research Development Co | Fluid catalytic cracking process with a segregated feed charged to the reactor |
| US3894932A (en) | 1973-11-19 | 1975-07-15 | Mobil Oil Corp | Conversion of hydrocarbons with {37 y{38 {0 faujasite-type catalysts |
| US3894936A (en) | 1973-11-19 | 1975-07-15 | Mobil Oil Corp | Conversion of hydrocarbons with {37 Y{38 {0 faujasite-type catalysts |
| US4002557A (en) | 1974-05-28 | 1977-01-11 | Mobil Oil Corporation | Catalytic conversion of high metals feed stocks |
| US4097243A (en) | 1976-11-04 | 1978-06-27 | Uop Inc. | Hydrocarbon-feed distributor of injecting hydrocarbon feed |
| US4268416A (en) * | 1979-06-15 | 1981-05-19 | Uop Inc. | Gaseous passivation of metal contaminants on cracking catalyst |
| US4332673A (en) | 1979-11-14 | 1982-06-01 | Ashland Oil, Inc. | High metal carbo-metallic oil conversion |
| US4347122A (en) * | 1979-11-14 | 1982-08-31 | Ashland Oil, Inc. | Carbo-metallic oil conversion with liquid water |
| US4341624A (en) | 1979-11-14 | 1982-07-27 | Ashland Oil, Inc. | Carbo-metallic oil conversion |
| US4376038A (en) * | 1979-11-14 | 1983-03-08 | Ashland Oil, Inc. | Use of naphtha as riser diluent in carbo-metallic oil conversion |
| US4280895A (en) * | 1979-12-31 | 1981-07-28 | Exxon Research & Engineering Co. | Passivation of cracking catalysts |
| US4316794A (en) | 1980-03-06 | 1982-02-23 | Mobil Oil Corporation | Direct conversion of residual oils |
| AU7325081A (en) * | 1981-05-13 | 1982-12-07 | Ashland Oil, Inc. | Steam reforming of carbo-metallic oils |
-
1982
- 1982-08-19 US US06/411,719 patent/US4435279A/en not_active Expired - Fee Related
-
1983
- 1983-07-06 EP EP83106610A patent/EP0101553A3/en not_active Withdrawn
- 1983-07-14 CA CA000432415A patent/CA1205407A/en not_active Expired
- 1983-08-17 JP JP58150100A patent/JPS5953591A/ja active Granted
Non-Patent Citations (1)
| Title |
|---|
| THE OIL AND GAS JOURNAL=1969 * |
Also Published As
| Publication number | Publication date |
|---|---|
| US4435279A (en) | 1984-03-06 |
| CA1205407A (en) | 1986-06-03 |
| JPS5953591A (ja) | 1984-03-28 |
| EP0101553A3 (en) | 1984-06-06 |
| EP0101553A2 (en) | 1984-02-29 |
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