DE2801373A1 - Katalytisches wirbelbett-crack-verfahren - Google Patents
Katalytisches wirbelbett-crack-verfahrenInfo
- Publication number
- DE2801373A1 DE2801373A1 DE19782801373 DE2801373A DE2801373A1 DE 2801373 A1 DE2801373 A1 DE 2801373A1 DE 19782801373 DE19782801373 DE 19782801373 DE 2801373 A DE2801373 A DE 2801373A DE 2801373 A1 DE2801373 A1 DE 2801373A1
- Authority
- DE
- Germany
- Prior art keywords
- catalyst
- zone
- starting product
- spent catalyst
- oil
- 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.)
- Withdrawn
Links
- 238000000034 method Methods 0.000 title claims description 35
- 230000008569 process Effects 0.000 title claims description 24
- 230000003197 catalytic effect Effects 0.000 title claims description 13
- 239000003054 catalyst Substances 0.000 claims description 257
- 239000000047 product Substances 0.000 claims description 120
- 238000006243 chemical reaction Methods 0.000 claims description 117
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 claims description 47
- 229930195733 hydrocarbon Natural products 0.000 claims description 45
- 150000002430 hydrocarbons Chemical class 0.000 claims description 44
- 239000004215 Carbon black (E152) Substances 0.000 claims description 39
- 239000000571 coke Substances 0.000 claims description 39
- 229910052799 carbon Inorganic materials 0.000 claims description 24
- 239000012535 impurity Substances 0.000 claims description 24
- 229910052757 nitrogen Inorganic materials 0.000 claims description 24
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 23
- 230000008929 regeneration Effects 0.000 claims description 22
- 238000011069 regeneration method Methods 0.000 claims description 22
- 239000000203 mixture Substances 0.000 claims description 17
- 238000000926 separation method Methods 0.000 claims description 11
- 238000004523 catalytic cracking Methods 0.000 claims description 9
- 239000002244 precipitate Substances 0.000 claims description 6
- 239000003085 diluting agent Substances 0.000 claims description 3
- 238000004231 fluid catalytic cracking Methods 0.000 claims description 3
- 230000003647 oxidation Effects 0.000 claims description 3
- 238000007254 oxidation reaction Methods 0.000 claims description 3
- 238000003197 gene knockdown Methods 0.000 claims description 2
- 238000002955 isolation Methods 0.000 claims description 2
- 238000010790 dilution Methods 0.000 claims 1
- 239000012895 dilution Substances 0.000 claims 1
- 150000002500 ions Chemical class 0.000 claims 1
- 239000003921 oil Substances 0.000 description 85
- 230000000694 effects Effects 0.000 description 30
- 238000005336 cracking Methods 0.000 description 27
- 239000007789 gas Substances 0.000 description 25
- 238000002474 experimental method Methods 0.000 description 14
- 229910021536 Zeolite Inorganic materials 0.000 description 10
- HNPSIPDUKPIQMN-UHFFFAOYSA-N dioxosilane;oxo(oxoalumanyloxy)alumane Chemical compound O=[Si]=O.O=[Al]O[Al]=O HNPSIPDUKPIQMN-UHFFFAOYSA-N 0.000 description 10
- 239000003502 gasoline Substances 0.000 description 10
- 239000010457 zeolite Substances 0.000 description 10
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 8
- 230000001105 regulatory effect Effects 0.000 description 8
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 6
- 150000001875 compounds Chemical class 0.000 description 6
- 239000010779 crude oil Substances 0.000 description 6
- 239000001301 oxygen Substances 0.000 description 6
- 229910052760 oxygen Inorganic materials 0.000 description 6
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 description 5
- 229910002091 carbon monoxide Inorganic materials 0.000 description 5
- 230000002411 adverse Effects 0.000 description 4
- 229910002092 carbon dioxide Inorganic materials 0.000 description 4
- 239000001569 carbon dioxide 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
- 239000007858 starting material Substances 0.000 description 4
- 230000008021 deposition Effects 0.000 description 3
- 239000000463 material Substances 0.000 description 3
- 150000002736 metal compounds Chemical class 0.000 description 3
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 2
- PXHVJJICTQNCMI-UHFFFAOYSA-N Nickel Chemical compound [Ni] PXHVJJICTQNCMI-UHFFFAOYSA-N 0.000 description 2
- SMWDFEZZVXVKRB-UHFFFAOYSA-N Quinoline Chemical compound N1=CC=CC2=CC=CC=C21 SMWDFEZZVXVKRB-UHFFFAOYSA-N 0.000 description 2
- 230000009471 action Effects 0.000 description 2
- 238000009835 boiling Methods 0.000 description 2
- 239000006227 byproduct Substances 0.000 description 2
- 238000011109 contamination Methods 0.000 description 2
- 230000009849 deactivation Effects 0.000 description 2
- 238000000605 extraction Methods 0.000 description 2
- 239000000446 fuel Substances 0.000 description 2
- 229910052698 phosphorus Inorganic materials 0.000 description 2
- 238000000746 purification Methods 0.000 description 2
- -1 steam Chemical compound 0.000 description 2
- 238000012360 testing method Methods 0.000 description 2
- XUKUURHRXDUEBC-KAYWLYCHSA-N Atorvastatin Chemical compound C=1C=CC=CC=1C1=C(C=2C=CC(F)=CC=2)N(CC[C@@H](O)C[C@@H](O)CC(O)=O)C(C(C)C)=C1C(=O)NC1=CC=CC=C1 XUKUURHRXDUEBC-KAYWLYCHSA-N 0.000 description 1
- ZOXJGFHDIHLPTG-UHFFFAOYSA-N Boron Chemical compound [B] ZOXJGFHDIHLPTG-UHFFFAOYSA-N 0.000 description 1
- 240000006890 Erythroxylum coca Species 0.000 description 1
- 241001026509 Kata Species 0.000 description 1
- MMOXZBCLCQITDF-UHFFFAOYSA-N N,N-diethyl-m-toluamide Chemical compound CCN(CC)C(=O)C1=CC=CC(C)=C1 MMOXZBCLCQITDF-UHFFFAOYSA-N 0.000 description 1
- 108010020943 Nitrogenase Proteins 0.000 description 1
- OFBQJSOFQDEBGM-UHFFFAOYSA-N Pentane Chemical class CCCCC OFBQJSOFQDEBGM-UHFFFAOYSA-N 0.000 description 1
- 239000002253 acid Substances 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
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 description 1
- 229910021529 ammonia Inorganic materials 0.000 description 1
- 125000003118 aryl group Chemical group 0.000 description 1
- 238000000889 atomisation Methods 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 229910052796 boron Inorganic materials 0.000 description 1
- 150000001722 carbon compounds Chemical class 0.000 description 1
- 239000004927 clay Substances 0.000 description 1
- 239000003245 coal Substances 0.000 description 1
- 235000008957 cocaer Nutrition 0.000 description 1
- ZPUCINDJVBIVPJ-LJISPDSOSA-N cocaine Chemical compound O([C@H]1C[C@@H]2CC[C@@H](N2C)[C@H]1C(=O)OC)C(=O)C1=CC=CC=C1 ZPUCINDJVBIVPJ-LJISPDSOSA-N 0.000 description 1
- 238000002485 combustion reaction Methods 0.000 description 1
- 238000004891 communication Methods 0.000 description 1
- 239000000356 contaminant Substances 0.000 description 1
- 230000001419 dependent effect Effects 0.000 description 1
- 238000013461 design Methods 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- 230000018109 developmental process Effects 0.000 description 1
- 150000001993 dienes Chemical class 0.000 description 1
- 239000003344 environmental pollutant Substances 0.000 description 1
- 238000001704 evaporation Methods 0.000 description 1
- 230000008020 evaporation Effects 0.000 description 1
- 230000029142 excretion Effects 0.000 description 1
- 239000000295 fuel oil Substances 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 150000002483 hydrogen compounds Chemical class 0.000 description 1
- 230000001771 impaired effect Effects 0.000 description 1
- 230000006872 improvement Effects 0.000 description 1
- 230000000968 intestinal effect Effects 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- CPLXHLVBOLITMK-UHFFFAOYSA-N magnesium oxide Inorganic materials [Mg]=O CPLXHLVBOLITMK-UHFFFAOYSA-N 0.000 description 1
- 239000000395 magnesium oxide Substances 0.000 description 1
- 229910044991 metal oxide Inorganic materials 0.000 description 1
- 150000004706 metal oxides Chemical class 0.000 description 1
- 229910052759 nickel Inorganic materials 0.000 description 1
- 150000002829 nitrogen Chemical class 0.000 description 1
- 229910017464 nitrogen compound Inorganic materials 0.000 description 1
- 150000002830 nitrogen compounds Chemical class 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 239000003208 petroleum Substances 0.000 description 1
- 231100000719 pollutant Toxicity 0.000 description 1
- 239000002243 precursor Substances 0.000 description 1
- 238000012545 processing Methods 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 239000011541 reaction mixture Substances 0.000 description 1
- 230000001172 regenerating effect Effects 0.000 description 1
- 239000010802 sludge Substances 0.000 description 1
- 229910052720 vanadium Inorganic materials 0.000 description 1
- GPPXJZIENCGNKB-UHFFFAOYSA-N vanadium Chemical compound [V]#[V] GPPXJZIENCGNKB-UHFFFAOYSA-N 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
- B01J8/18—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles
- B01J8/24—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles according to "fluidised-bed" technique
- B01J8/26—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles according to "fluidised-bed" technique with two or more fluidised beds, e.g. reactor and regeneration installations
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Organic Chemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Combustion & Propulsion (AREA)
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
- Catalysts (AREA)
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US05/760,247 US4090948A (en) | 1977-01-17 | 1977-01-17 | Catalytic cracking process |
Publications (1)
Publication Number | Publication Date |
---|---|
DE2801373A1 true DE2801373A1 (de) | 1978-07-20 |
Family
ID=25058524
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
DE19782801373 Withdrawn DE2801373A1 (de) | 1977-01-17 | 1978-01-13 | Katalytisches wirbelbett-crack-verfahren |
Country Status (7)
Country | Link |
---|---|
US (1) | US4090948A (en, 2012) |
BR (1) | BR7800228A (en, 2012) |
CA (1) | CA1125687A (en, 2012) |
DE (1) | DE2801373A1 (en, 2012) |
FR (1) | FR2377443A1 (en, 2012) |
GB (1) | GB1591682A (en, 2012) |
MX (1) | MX148381A (en, 2012) |
Families Citing this family (43)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4257875A (en) * | 1979-05-29 | 1981-03-24 | Uop Inc. | Fluid catalytic cracking process |
US4390503A (en) * | 1981-05-13 | 1983-06-28 | Ashland Oil, Inc. | Carbometallic oil conversion with ballistic separation |
US4419219A (en) * | 1981-09-24 | 1983-12-06 | Exxon Research And Engineering Co. | Adsorption of basic asphaltenes on solid acid catalysts |
US4422926A (en) * | 1981-09-24 | 1983-12-27 | Exxon Research And Engineering Co. | Separating basic asphaltenes using Bronsted acid transition metal oxide acid catalysts |
US4424114A (en) | 1981-09-24 | 1984-01-03 | Exxon Research And Engineering Co. | Separating basic asphaltenes using transition metal oxide acid catalysts |
AT379610B (de) * | 1982-03-29 | 1986-02-10 | Engelhard Corp | Verfahren und vorrichtung zum entkarbonisieren und entmetallisieren schwerer rohoelfraktionen |
US4417974A (en) * | 1982-08-23 | 1983-11-29 | Chevron Research Company | Riser cracking of catalyst-deactivating feeds |
EP0180291A1 (en) * | 1984-10-26 | 1986-05-07 | Mobil Oil Corporation | Feed mixing technique for fluidized catalytic cracking of hydrocarbon oil |
US4747935A (en) * | 1986-03-26 | 1988-05-31 | Union Oil Company Of California | Process for the catalytic cracking of feedstocks containing nitrogen |
US4708786A (en) * | 1986-03-26 | 1987-11-24 | Union Oil Company Of California | Process for the catalytic cracking of nitrogen-containing feedstocks |
US4871446A (en) * | 1986-09-03 | 1989-10-03 | Mobil Oil Corporation | Catalytic cracking process employing mixed catalyst system |
DE3782221T2 (de) * | 1986-09-03 | 1993-05-06 | Mobil Oil Corp | Strippverfahren fuer einen katalysator aus eine katalytische spaltzone. |
US4880521A (en) * | 1987-05-07 | 1989-11-14 | Union Oil Company Of California | Process for the cracking of feedstocks containing high levels of nitrogen |
US4810369A (en) * | 1987-05-07 | 1989-03-07 | Union Oil Company Of California | Process for the catalytic cracking of feedstocks containing high levels of nitrogen |
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 |
US5372704A (en) * | 1990-05-24 | 1994-12-13 | Mobil Oil Corporation | Cracking with spent catalyst |
US5154818A (en) * | 1990-05-24 | 1992-10-13 | Mobil Oil Corporation | Multiple zone catalytic cracking of hydrocarbons |
US6023005A (en) * | 1997-07-03 | 2000-02-08 | Exxon Chemicals Patents Inc. | Process for converting oxygenates to olefins using molecular sieve catalysts comprising desirable carbonaceous deposits |
US6113776A (en) | 1998-06-08 | 2000-09-05 | Uop Llc | FCC process with high temperature cracking zone |
CN1081222C (zh) | 1999-06-23 | 2002-03-20 | 中国石油化工集团公司 | 一种降低液化气和汽油中烯烃含量的催化转化方法 |
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 |
EP3225678B1 (en) | 2004-03-08 | 2022-04-27 | China Petroleum & Chemical Corporation | Am fcc process with two reaction zones |
US8202412B2 (en) * | 2007-07-17 | 2012-06-19 | Exxonmobil Research And Engineering Company | Reduced elevation catalyst return line for a fluid catalytic cracking unit |
KR101589565B1 (ko) * | 2007-12-20 | 2016-01-28 | 차이나 페트로리움 앤드 케미컬 코포레이션 | 탄화수소유의 수소화처리 및 촉매식 분해의 결합된 방법 |
US8288599B2 (en) | 2008-06-30 | 2012-10-16 | Kior, Inc. | Co-processing solid biomass in a conventional petroleum refining process unit |
WO2010002886A1 (en) * | 2008-06-30 | 2010-01-07 | Kior, Inc. | Producing fuel and speciality chemicals from biomass containing triglycerides and cellulose |
US8007728B2 (en) * | 2008-12-11 | 2011-08-30 | Uop Llc | System, apparatus, and process for cracking a hydrocarbon feed |
US8137631B2 (en) * | 2008-12-11 | 2012-03-20 | Uop Llc | Unit, system and process for catalytic cracking |
US8940955B2 (en) * | 2008-12-19 | 2015-01-27 | Uop Llc | Fluid catalytic cracking system and process |
US8246914B2 (en) * | 2008-12-22 | 2012-08-21 | Uop Llc | Fluid catalytic cracking system |
US8889076B2 (en) * | 2008-12-29 | 2014-11-18 | Uop Llc | Fluid catalytic cracking system and process |
US9284495B2 (en) * | 2009-03-20 | 2016-03-15 | Uop Llc | Maintaining catalyst activity for converting a hydrocarbon feed |
US20100243528A1 (en) * | 2009-03-30 | 2010-09-30 | Bell Leonard E | Method and system relating to a wet gas compressor |
US8796496B2 (en) * | 2009-09-03 | 2014-08-05 | Basf Se | Process for preparing benzene from methane |
US8702971B2 (en) | 2010-03-31 | 2014-04-22 | Uop Llc | Process and apparatus for alkylating and hydrogenating a light cycle oil |
US9017428B2 (en) | 2010-11-16 | 2015-04-28 | Kior, Inc. | Two-stage reactor and process for conversion of solid biomass material |
EP2756057A4 (en) * | 2011-09-15 | 2015-06-24 | Chevron Usa Inc | HYDROPROCESSING CATALYSTS AND MANUFACTURING METHOD THEREFOR |
CA2862414C (en) | 2012-01-06 | 2020-07-07 | Kior, Inc. | Two-stage reactor and process for conversion of solid biomass material |
US8691077B2 (en) | 2012-03-13 | 2014-04-08 | Uop Llc | Process for converting a hydrocarbon stream, and optionally producing a hydrocracked distillate |
US8864979B2 (en) | 2012-03-21 | 2014-10-21 | Uop Llc | Process and apparatus for fluid catalytic cracking |
CN105586080B (zh) * | 2014-10-20 | 2017-07-25 | 中国石油化工股份有限公司 | 一种页岩油催化裂化的加工方法 |
CN106590735B (zh) * | 2015-10-15 | 2019-09-24 | 中国石油化工股份有限公司 | 一种催化裂化方法和装置 |
CN110724553B (zh) * | 2018-07-16 | 2021-04-06 | 中国石油化工股份有限公司 | 一种采用稀相输送床与快速流化床进行催化裂解的方法和系统 |
Citations (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2312230A (en) * | 1940-06-29 | 1943-02-23 | Kellogg M W Co | Catalytic conversion of hydrocarbons |
US2439811A (en) * | 1941-05-21 | 1948-04-20 | Kellogg M W Co | Catalytic conversion of hydrocarbons |
US2487132A (en) * | 1944-12-09 | 1949-11-08 | Standard Oil Dev Co | Contacting gaseous fluid with solid particles |
US2700015A (en) * | 1950-11-10 | 1955-01-18 | Gulf Research Development Co | High pressure fluid hydrogenation process |
US2847364A (en) * | 1952-09-12 | 1958-08-12 | Gulf Research Development Co | Process for conversion of hydrocarbons and for transport of solid particles |
US2892773A (en) * | 1953-12-29 | 1959-06-30 | Gulf Research Development Co | Fluidized process and apparatus for the transfer of solids in a fluidized system |
US2965454A (en) * | 1957-04-30 | 1960-12-20 | Phillips Petroleum Co | Fluidized conversion and stripping apparatus |
Family Cites Families (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2379159A (en) * | 1943-07-31 | 1945-06-26 | Universal Oil Prod Co | Process for the catalytic conversion of hydrocarbons |
US3186805A (en) * | 1961-11-06 | 1965-06-01 | Phillips Petroleum Co | Catalytic apparatus |
US3380911A (en) * | 1966-02-15 | 1968-04-30 | Mobil Oil Corp | Method for converting hydrocarbons in two stages |
US3639228A (en) * | 1969-10-28 | 1972-02-01 | Gulf Research Development Co | Fcc process utilizing divided catalyst injection |
US3679576A (en) * | 1970-01-06 | 1972-07-25 | Commw Oil Refining Co Inc | Fluidized catalytic cracking apparatus and process |
US3888762A (en) * | 1972-10-12 | 1975-06-10 | Universal Oil Prod Co | Fluid catalytic cracking process |
US3812029A (en) * | 1972-10-13 | 1974-05-21 | Mobil Oil Corp | Device for injecting easily coked fluids into a high temperature vessel |
US3997428A (en) * | 1974-05-06 | 1976-12-14 | Phillips Petroleum Company | Vaporization of oil feed by addition of regenerated catalyst |
-
1977
- 1977-01-17 US US05/760,247 patent/US4090948A/en not_active Expired - Lifetime
-
1978
- 1978-01-12 CA CA294,869A patent/CA1125687A/en not_active Expired
- 1978-01-13 BR BR7800228A patent/BR7800228A/pt unknown
- 1978-01-13 FR FR7800906A patent/FR2377443A1/fr active Granted
- 1978-01-13 DE DE19782801373 patent/DE2801373A1/de not_active Withdrawn
- 1978-01-16 GB GB1621/78A patent/GB1591682A/en not_active Expired
- 1978-01-17 MX MX172075A patent/MX148381A/es unknown
Patent Citations (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2312230A (en) * | 1940-06-29 | 1943-02-23 | Kellogg M W Co | Catalytic conversion of hydrocarbons |
US2439811A (en) * | 1941-05-21 | 1948-04-20 | Kellogg M W Co | Catalytic conversion of hydrocarbons |
US2487132A (en) * | 1944-12-09 | 1949-11-08 | Standard Oil Dev Co | Contacting gaseous fluid with solid particles |
US2700015A (en) * | 1950-11-10 | 1955-01-18 | Gulf Research Development Co | High pressure fluid hydrogenation process |
US2847364A (en) * | 1952-09-12 | 1958-08-12 | Gulf Research Development Co | Process for conversion of hydrocarbons and for transport of solid particles |
US2892773A (en) * | 1953-12-29 | 1959-06-30 | Gulf Research Development Co | Fluidized process and apparatus for the transfer of solids in a fluidized system |
US2965454A (en) * | 1957-04-30 | 1960-12-20 | Phillips Petroleum Co | Fluidized conversion and stripping apparatus |
Also Published As
Publication number | Publication date |
---|---|
BR7800228A (pt) | 1978-09-05 |
CA1125687A (en) | 1982-06-15 |
FR2377443B1 (en, 2012) | 1984-11-09 |
GB1591682A (en) | 1981-06-24 |
FR2377443A1 (fr) | 1978-08-11 |
MX148381A (es) | 1983-04-18 |
US4090948A (en) | 1978-05-23 |
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