AU4311185A - Residual oil cracking process using dry gas as lift gas initially in riser reactor - Google Patents
Residual oil cracking process using dry gas as lift gas initially in riser reactorInfo
- Publication number
- AU4311185A AU4311185A AU43111/85A AU4311185A AU4311185A AU 4311185 A AU4311185 A AU 4311185A AU 43111/85 A AU43111/85 A AU 43111/85A AU 4311185 A AU4311185 A AU 4311185A AU 4311185 A AU4311185 A AU 4311185A
- Authority
- AU
- Australia
- Prior art keywords
- gas
- lift gas
- catalyst
- cracking process
- oil cracking
- 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.)
- Granted
Links
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
- C10G47/00—Cracking of hydrocarbon oils, in the presence of hydrogen or hydrogen- generating compounds, to obtain lower boiling fractions
- C10G47/24—Cracking of hydrocarbon oils, in the presence of hydrogen or hydrogen- generating compounds, to obtain lower boiling fractions with moving solid particles
- C10G47/30—Cracking of hydrocarbon oils, in the presence of hydrogen or hydrogen- generating compounds, to obtain lower boiling fractions with moving solid particles according to the "fluidised-bed" technique
-
- 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)
Abstract
Dry gas (containing little C3+ and almost no C5+) is substituted for wet gas (generally containing C3+ and C5+) and used as the lift gas for transporting catalyst through a hydrocarbon conversion riser e.g. metal removal system, fluid catalytic cracker, and RCC<sm> heavy oil cracking process. Preferably the hydrocarbon feed contact the catalyst-lift gas mixture after some period of acceleration and mixing and passivation of contaminants on the catalyst surface. Advantages include lower gasing and lower coke-make as well as better product selectivity. Preferred catalyst-lift gas contact times are from about 0.01 to 2, more preferably 0.05 to 1.5, and most preferably 0.15 to 1 second. Preferred lift gas hydrogen contents are at least about 10, more preferably 15 and most preferably 20 mol precent hydrogen.
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US62019684A | 1984-06-13 | 1984-06-13 | |
US620196 | 1996-03-22 |
Publications (2)
Publication Number | Publication Date |
---|---|
AU4311185A true AU4311185A (en) | 1985-12-19 |
AU588528B2 AU588528B2 (en) | 1989-09-21 |
Family
ID=24484979
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
AU43111/85A Ceased AU588528B2 (en) | 1984-06-13 | 1985-05-29 | Residual oil cracking process using dry gas as lift gas initially in riser reactor |
Country Status (9)
Country | Link |
---|---|
EP (1) | EP0171460B1 (en) |
JP (1) | JPS614785A (en) |
AT (1) | ATE36554T1 (en) |
AU (1) | AU588528B2 (en) |
CA (1) | CA1265464A (en) |
DE (1) | DE3473473D1 (en) |
IN (1) | IN162877B (en) |
MX (1) | MX165471B (en) |
RU (1) | RU2091433C1 (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN109297742A (en) * | 2018-11-21 | 2019-02-01 | 上海市计量测试技术研究院 | Kitchen fumes generator |
Families Citing this family (27)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH0662958B2 (en) * | 1985-02-28 | 1994-08-17 | 富士スタンダ−ドリサ−チ株式会社 | Pyrolysis of heavy oil |
US4853105A (en) * | 1986-09-03 | 1989-08-01 | Mobil Oil Corporation | Multiple riser fluidized catalytic cracking process utilizing hydrogen and carbon-hydrogen contributing fragments |
US4802971A (en) * | 1986-09-03 | 1989-02-07 | Mobil Oil Corporation | Single 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 |
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 |
EP0280724A4 (en) * | 1986-09-03 | 1989-10-25 | Mobil Oil Corp | Processing of activated heavy hydrocarbon feeds. |
JPS6384632A (en) * | 1986-09-03 | 1988-04-15 | モービル・オイル・コーポレイション | Fluid catalytic cracking method |
US4957617A (en) * | 1986-09-03 | 1990-09-18 | Mobil Oil Corporation | Fluid catalytic cracking |
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 |
FR2624762B1 (en) * | 1987-12-21 | 1990-06-08 | Total France | METHOD AND DEVICE FOR REGENERATING A FLUIDIZED BED CATALYST |
FR2625509B1 (en) * | 1987-12-30 | 1990-06-22 | Total France | METHOD AND DEVICE FOR CONVERTING HYDROCARBONS INTO A FLUIDIZED BED |
US5264115A (en) * | 1987-12-30 | 1993-11-23 | Compagnie De Raffinage Et De Distribution Total France | Process and apparatus for fluidized bed hydrocarbon conversion |
FR2628436B1 (en) * | 1988-03-10 | 1992-04-24 | Total France | METHOD AND DEVICE FOR VAPOCRACKING HYDROCARBONS IN FLUIDIZED PHASE OF HEAT-CARRYING PARTICLES |
EP1046696B1 (en) * | 1999-04-23 | 2014-06-11 | China Petrochemical Corporation | A catalytic conversion process for producing isobutane and isoparaffin-enriched gasoline |
CN1078094C (en) | 1999-04-23 | 2002-01-23 | 中国石油化工集团公司 | Lift pipe reactor for fluidized catalytic conversion |
JP4859358B2 (en) * | 2004-09-22 | 2012-01-25 | 日揮触媒化成株式会社 | Catalytic cracking gasoline desulfurization catalyst and catalytic cracking gasoline desulfurization method using the same |
CN1986505B (en) | 2005-12-23 | 2010-04-14 | 中国石油化工股份有限公司 | Catalytic conversion process with increased low carbon olefine output |
MX2008016078A (en) * | 2006-06-22 | 2009-01-15 | Shell Int Research | Methods for producing a crude product from selected feed. |
CN101952394B (en) * | 2007-10-10 | 2013-09-11 | 国际壳牌研究有限公司 | Systems and methods for making a middle distillate product and lower olefins from a hydrocarbon feedstock |
EP2231821A1 (en) * | 2007-11-29 | 2010-09-29 | Shell Internationale Research Maatschappij B.V. | Systems and methods for making a middle distillate product and lower olefins from a hydrocarbon feedstock |
US9157037B2 (en) | 2008-12-18 | 2015-10-13 | Uop Llc | Process for improving flow properties of crude petroleum |
US8263008B2 (en) | 2008-12-18 | 2012-09-11 | Uop Llc | Apparatus for improving flow properties of crude petroleum |
FR2953851B1 (en) * | 2009-12-14 | 2012-12-21 | Total Raffinage Marketing | CATALYTIC CRACKING PROCESS WITH MAXIMIZATION OF GAS BASES |
FR2966160B1 (en) * | 2010-10-14 | 2013-11-15 | IFP Energies Nouvelles | CATALYTIC CRACKING METHOD FOR PROCESSING LOW CARBON CONRADSON LOADS COMPRISING THE RECYCLING OF A CUTTING CUTTING ACCORDING TO A NEW TECHNOLOGY |
CN103827262B (en) | 2011-07-29 | 2015-12-23 | 沙特***石油公司 | For the rich hydrogen raw material of fluidized catalytic cracking method |
US11286429B2 (en) | 2020-06-25 | 2022-03-29 | Saudi Arabian Oil Company | Process for heavy oil upgrading utilizing hydrogen and water |
WO2024059600A1 (en) * | 2022-09-14 | 2024-03-21 | Dow Global Technologies Llc | Methods for dehydrogenating hydrocarbons utilizing regenerators |
Family Cites Families (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3894932A (en) * | 1973-11-19 | 1975-07-15 | Mobil Oil Corp | Conversion of hydrocarbons with {37 y{38 {0 faujasite-type catalysts |
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 |
US4336160A (en) * | 1980-07-15 | 1982-06-22 | Dean Robert R | Method and apparatus for cracking residual oils |
US4432863A (en) * | 1981-07-20 | 1984-02-21 | Ashland Oil, Inc. | Steam reforming of carbo-metallic oils |
US4508839A (en) * | 1981-08-27 | 1985-04-02 | Ashland Oil, Inc. | Catalyst for the conversion of carbo-metallic containing oils |
US4457833A (en) * | 1981-08-27 | 1984-07-03 | Ashland Oil, Inc. | Process and catalyst for the conversion of carbo-metallic containing oils |
US4427537A (en) * | 1982-03-17 | 1984-01-24 | Dean Robert R | Method and means for preparing and dispersing atomed hydrocarbon with fluid catalyst particles in a reactor zone |
US4427539A (en) * | 1982-09-07 | 1984-01-24 | Ashland Oil, Inc. | Demetallizing and decarbonizing heavy residual oil feeds |
US4479870A (en) * | 1984-02-29 | 1984-10-30 | Jop Inc. | Use of lift gas in an FCC reactor riser |
-
1984
- 1984-10-25 IN IN827/DEL/84A patent/IN162877B/en unknown
- 1984-10-30 CA CA000466631A patent/CA1265464A/en not_active Expired - Lifetime
- 1984-12-17 EP EP84112717A patent/EP0171460B1/en not_active Expired
- 1984-12-17 AT AT84112717T patent/ATE36554T1/en not_active IP Right Cessation
- 1984-12-17 DE DE8484112717T patent/DE3473473D1/en not_active Expired
-
1985
- 1985-02-21 JP JP60033649A patent/JPS614785A/en active Granted
- 1985-05-29 AU AU43111/85A patent/AU588528B2/en not_active Ceased
- 1985-06-06 MX MX205562A patent/MX165471B/en unknown
- 1985-06-12 RU SU853911820A patent/RU2091433C1/en active
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN109297742A (en) * | 2018-11-21 | 2019-02-01 | 上海市计量测试技术研究院 | Kitchen fumes generator |
CN109297742B (en) * | 2018-11-21 | 2024-03-12 | 上海市计量测试技术研究院 | Cooking fume generator |
Also Published As
Publication number | Publication date |
---|---|
MX165471B (en) | 1992-11-12 |
ATE36554T1 (en) | 1988-09-15 |
RU2091433C1 (en) | 1997-09-27 |
EP0171460B1 (en) | 1988-08-17 |
JPS614785A (en) | 1986-01-10 |
CA1265464A (en) | 1990-02-06 |
AU588528B2 (en) | 1989-09-21 |
JPH0226663B2 (en) | 1990-06-12 |
EP0171460A1 (en) | 1986-02-19 |
IN162877B (en) | 1988-07-16 |
DE3473473D1 (en) | 1988-09-22 |
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Legal Events
Date | Code | Title | Description |
---|---|---|---|
MK14 | Patent ceased section 143(a) (annual fees not paid) or expired |