ES8107293A1 - Metodo para transfomar petroleos y similares en productos menos pesados - Google Patents
Metodo para transfomar petroleos y similares en productos menos pesadosInfo
- Publication number
- ES8107293A1 ES8107293A1 ES497230A ES497230A ES8107293A1 ES 8107293 A1 ES8107293 A1 ES 8107293A1 ES 497230 A ES497230 A ES 497230A ES 497230 A ES497230 A ES 497230A ES 8107293 A1 ES8107293 A1 ES 8107293A1
- Authority
- ES
- Spain
- Prior art keywords
- carbo
- oils
- metallic
- crude
- reduced crude
- 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
Classifications
-
- 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
- B01J29/00—Catalysts comprising molecular sieves
- B01J29/90—Regeneration or reactivation
-
- 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
- B01J29/00—Catalysts comprising molecular sieves
- B01J29/04—Catalysts comprising molecular sieves having base-exchange properties, e.g. crystalline zeolites
- B01J29/06—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof
-
- 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
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P30/00—Technologies relating to oil refining and petrochemical industry
- Y02P30/40—Ethylene production
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Materials Engineering (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Crystallography & Structural Chemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
Abstract
PROCEDIMIENTO PARA LA CONVERSION CATALITICA CONTINUA DE CRUDOS O ACEITES MINERALES, DE ORIGEN PETROLIFERO O NO, CON ALTO CONTENIDO EN NIQUEL Y/O OTROS METALES, A PRODUCTOS DE PESO MOLECULAR MAS BAJO, TALES COMO GASOLINAS. CONSISTENTE EN LA CONVERSION DE UNA ALIMENTACION CARBOMETALICA, QUE COMPRENDE PETROLEO, QUE HIERVE A PARTIR DE 343GC, CARACTERIZANDOSE ESTA PORCION POR UN CONTENIDO DE EQUIVALENTE EN NIQUEL COMPRENDIDO ENTRE 4 Y 5,5 PPM EN PESO Y POR UN RESIDUO DE CARBONO A LA PIROLISIS ENTRE 1 Y 2 POR 100 EN PESO. LA ALIMENTACION SE MEZCLA CON CATALIZADOR CALIENTE DE CONVERSION. TAMBIEN PUEDE AGREGARSE MATERIAL GASEOSO QUE INCLUYE VAPOR DE AGUA. EL REACTOR ES DE CIRCULACION PROGRESIVA Y LA CONVERSION TIENE LUGAR A TEMPERATURA ENTRE 482 Y 760GC Y PRESION ENTRE 0,7 Y 3,5 KG/CM CUADRADOS, OBTENIENDOSE UNA CONVERSION DE 50 POR 100 O MAS. EL CATALIZADOR SE SEPARA DE LA CORRIENTE DE HIDROCARBUROS DE ALIMENTACION Y PRODUCTOS DE CRAQUEO, Y A CONTINUACION ES RECTIFICADO, REGENERADO Y RECICLADO. LOS HIDROCARBUROS NO CRAQUEADOS EN LA PRIMERA PASADA SE PUEDEN RECICLAR. C
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US06/094,092 US4332673A (en) | 1979-11-14 | 1979-11-14 | High metal carbo-metallic oil conversion |
Publications (2)
Publication Number | Publication Date |
---|---|
ES8107293A1 true ES8107293A1 (es) | 1981-10-16 |
ES497230A0 ES497230A0 (es) | 1981-10-16 |
Family
ID=22242869
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
ES497230A Granted ES497230A0 (es) | 1979-11-14 | 1980-11-14 | Metodo para transfomar petroleos y similares en productos menos pesados |
Country Status (15)
Country | Link |
---|---|
US (1) | US4332673A (es) |
JP (1) | JPS5684790A (es) |
AT (1) | AT374817B (es) |
AU (1) | AU545834B2 (es) |
BR (1) | BR8007425A (es) |
CA (1) | CA1167793A (es) |
DE (1) | DE3043032A1 (es) |
EG (1) | EG15381A (es) |
ES (1) | ES497230A0 (es) |
GB (1) | GB2063294B (es) |
IL (1) | IL61491A (es) |
IN (1) | IN155030B (es) |
MX (1) | MX160983A (es) |
YU (1) | YU42542B (es) |
ZA (1) | ZA807031B (es) |
Families Citing this family (18)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4419223A (en) * | 1979-11-14 | 1983-12-06 | Ashland Oil, Inc. | Carbo-metallic oil conversion with water |
US4431515A (en) * | 1979-11-14 | 1984-02-14 | Ashland Oil, Inc. | Carbometallic oil conversion with hydrogen in a riser using a high metals containing catalyst |
US4708785A (en) * | 1979-11-14 | 1987-11-24 | Ashland Oil, Inc. | Carbo-metallic oil conversion |
US4406773A (en) * | 1981-05-13 | 1983-09-27 | Ashland Oil, Inc. | Magnetic separation of high activity catalyst from low activity catalyst |
US4432863A (en) * | 1981-07-20 | 1984-02-21 | Ashland Oil, Inc. | Steam reforming of carbo-metallic oils |
US4464250A (en) * | 1981-07-30 | 1984-08-07 | Ashland Oil, Inc. | Stripping hydrocarbons from catalyst with combustion gases |
US4412914A (en) * | 1981-08-10 | 1983-11-01 | Ashland Oil, Inc. | Endothermic removal of coke deposited on sorbent materials during carbo-metallic oil conversion |
US4405445A (en) * | 1981-08-24 | 1983-09-20 | Ashland Oil, Inc. | Homogenization of water and reduced crude for catalytic cracking |
US4508839A (en) * | 1981-08-27 | 1985-04-02 | Ashland Oil, Inc. | Catalyst for the conversion of carbo-metallic containing oils |
US4894141A (en) * | 1981-09-01 | 1990-01-16 | Ashland Oil, Inc. | Combination process for upgrading residual oils |
US4569753A (en) * | 1981-09-01 | 1986-02-11 | Ashland Oil, Inc. | Oil upgrading by thermal and catalytic cracking |
USRE33728E (en) * | 1981-11-24 | 1991-10-29 | Total Engineering And Research Company | Method for catalytically converting residual oils |
US4435279A (en) | 1982-08-19 | 1984-03-06 | Ashland Oil, Inc. | Method and apparatus for converting oil feeds |
US4601814A (en) * | 1983-05-27 | 1986-07-22 | Total Engineering And Research Company | Method and apparatus for cracking residual oils |
US4859310A (en) * | 1988-03-25 | 1989-08-22 | Amoco Corporation | Catalytic cracking of whole crude oil |
US5190635A (en) * | 1989-04-03 | 1993-03-02 | Ashland Oil, Inc. | Superparamagnetic formation of FCC catalyst provides means of separation of old equilibrium fluid cracking catalyst |
US5171424A (en) * | 1990-10-22 | 1992-12-15 | Ashland Oil, Inc. | Magnetic separation of old from new cracking catalyst by means of heavy rare earth "magnetic hooks" |
US9315733B2 (en) * | 2006-10-20 | 2016-04-19 | Saudi Arabian Oil Company | Asphalt production from solvent deasphalting bottoms |
Family Cites Families (14)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2575258A (en) * | 1948-12-06 | 1951-11-13 | Standard Oil Dev Co | Regenerating an iron-contaminated cracking catalyst |
US3303123A (en) * | 1964-10-16 | 1967-02-07 | Phillips Petroleum Co | Catalytic cracking of residuum oils containing metal contaminants in several stages |
US3617512A (en) * | 1969-06-25 | 1971-11-02 | James R Murphy | Fluid catalytic cracking process |
US3767566A (en) * | 1970-01-26 | 1973-10-23 | Standard Oil Co | Catalytic petroleum conversion process |
US3785962A (en) * | 1971-12-27 | 1974-01-15 | Universal Oil Prod Co | Fluidized catalytic cracking process |
US4064038A (en) * | 1973-05-21 | 1977-12-20 | Universal Oil Products Company | Fluid catalytic cracking process for conversion of residual oils |
US3944482A (en) * | 1973-08-08 | 1976-03-16 | Gulf Research & Development Company | Process for the cracking of high metals content feedstocks |
US4013546A (en) * | 1974-07-19 | 1977-03-22 | Texaco Inc. | Removing metal contaminant from regenerated catalyst in catalytic cracking process |
US3974062A (en) * | 1974-10-17 | 1976-08-10 | Mobil Oil Corporation | Conversion of full range crude oils with low molecular weight carbon-hydrogen fragment contributors over zeolite catalysts |
AT364745B (de) * | 1975-03-24 | 1981-11-10 | Ashland Oil Inc | Verfahren und vorrichtung zum abscheiden feiner feststoffteilchen aus stroemenden gasen |
US4176084A (en) * | 1975-07-08 | 1979-11-27 | Exxon Research & Engineering Co. | Process for regenerating metal-contaminated hydrocarbon conversion catalysts |
US4162213A (en) * | 1976-04-29 | 1979-07-24 | Mobil Oil Corporation | Catalytic cracking of metal-contaminated oils |
US4200520A (en) * | 1978-01-30 | 1980-04-29 | Exxon Research & Engineering Co. | Catalytic cracking process |
US4233139A (en) * | 1978-07-25 | 1980-11-11 | Exxon Research & Engineering Co. | Acid catalyzed hydrocarbon conversion processes utilizing a catalyst comprising a Group IVB, VB or VIB metal oxide on an inorganic refractory oxide support |
-
1979
- 1979-11-14 US US06/094,092 patent/US4332673A/en not_active Expired - Lifetime
-
1980
- 1980-11-12 GB GB8036290A patent/GB2063294B/en not_active Expired
- 1980-11-13 BR BR8007425A patent/BR8007425A/pt not_active IP Right Cessation
- 1980-11-13 AT AT0559380A patent/AT374817B/de not_active IP Right Cessation
- 1980-11-13 ZA ZA00807031A patent/ZA807031B/xx unknown
- 1980-11-14 MX MX184791A patent/MX160983A/es unknown
- 1980-11-14 DE DE19803043032 patent/DE3043032A1/de active Granted
- 1980-11-14 ES ES497230A patent/ES497230A0/es active Granted
- 1980-11-14 YU YU2903/80A patent/YU42542B/xx unknown
- 1980-11-14 CA CA000364655A patent/CA1167793A/en not_active Expired
- 1980-11-14 JP JP15968780A patent/JPS5684790A/ja active Granted
- 1980-11-14 IN IN804/DEL/80A patent/IN155030B/en unknown
- 1980-11-14 AU AU64392/80A patent/AU545834B2/en not_active Ceased
- 1980-11-14 IL IL61491A patent/IL61491A/xx not_active IP Right Cessation
- 1980-11-15 EG EG713/80A patent/EG15381A/xx active
Also Published As
Publication number | Publication date |
---|---|
MX160983A (es) | 1990-06-29 |
GB2063294B (en) | 1984-04-26 |
GB2063294A (en) | 1981-06-03 |
JPS5684790A (en) | 1981-07-10 |
AU6439280A (en) | 1981-05-21 |
EG15381A (en) | 1991-06-30 |
YU290380A (en) | 1983-12-31 |
DE3043032A1 (de) | 1981-09-03 |
CA1167793A (en) | 1984-05-22 |
ATA559380A (de) | 1983-10-15 |
DE3043032C2 (es) | 1989-07-20 |
AT374817B (de) | 1984-06-12 |
ZA807031B (en) | 1982-01-27 |
YU42542B (en) | 1988-10-31 |
ES497230A0 (es) | 1981-10-16 |
AU545834B2 (en) | 1985-08-01 |
BR8007425A (pt) | 1981-05-26 |
US4332673A (en) | 1982-06-01 |
IN155030B (es) | 1984-12-22 |
JPH0116879B2 (es) | 1989-03-28 |
IL61491A (en) | 1984-04-30 |
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