IN162877B - - Google Patents
Info
- Publication number
- IN162877B IN162877B IN827/DEL/84A IN827DE1984A IN162877B IN 162877 B IN162877 B IN 162877B IN 827DE1984 A IN827DE1984 A IN 827DE1984A IN 162877 B IN162877 B IN 162877B
- Authority
- IN
- India
- Prior art keywords
- catalyst
- lift gas
- gas
- preferred
- hydrogen
- Prior art date
Links
- 239000007789 gas Substances 0.000 abstract 6
- 239000004215 Carbon black (E152) Substances 0.000 abstract 2
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 abstract 2
- 239000003054 catalyst Substances 0.000 abstract 2
- 229930195733 hydrocarbon Natural products 0.000 abstract 2
- 150000002430 hydrocarbons Chemical class 0.000 abstract 2
- 239000001257 hydrogen Substances 0.000 abstract 2
- 229910052739 hydrogen Inorganic materials 0.000 abstract 2
- 230000001133 acceleration Effects 0.000 abstract 1
- 230000003197 catalytic effect Effects 0.000 abstract 1
- 238000006243 chemical reaction Methods 0.000 abstract 1
- 239000000356 contaminant Substances 0.000 abstract 1
- 238000005336 cracking Methods 0.000 abstract 1
- 239000012530 fluid Substances 0.000 abstract 1
- 239000000295 fuel oil Substances 0.000 abstract 1
- 239000002184 metal Substances 0.000 abstract 1
- 238000000034 method Methods 0.000 abstract 1
- 239000000203 mixture Substances 0.000 abstract 1
- 238000002161 passivation Methods 0.000 abstract 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
- 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 (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US62019684A | 1984-06-13 | 1984-06-13 |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| IN162877B true IN162877B (en) | 1988-07-16 |
Family
ID=24484979
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| IN827/DEL/84A IN162877B (en) | 1984-06-13 | 1984-10-25 |
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) |
Families Citing this family (29)
| 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 |
| 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 |
| 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 |
| 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 |
| 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 |
| CA1302936C (en) * | 1986-09-03 | 1992-06-09 | Hartley Owen | Process for fluidized catalytic cracking with reactive fragments |
| 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 |
| 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 |
| EP1046696B1 (en) * | 1999-04-23 | 2014-06-11 | China Petrochemical Corporation | A catalytic conversion process for producing isobutane and isoparaffin-enriched gasoline |
| 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 | A catalytic conversion method for increasing production of low-carbon olefins |
| JP2009541537A (en) * | 2006-06-22 | 2009-11-26 | シエル・インターナシヨネイル・リサーチ・マーチヤツピイ・ベー・ウイ | Process for producing crude product from selected raw materials |
| DE112008002718T5 (en) * | 2007-10-10 | 2010-09-09 | Shell Internationale Research Maatschappij B.V. | Systems and processes for producing a middle distillate product and lower olefins from a hydrocarbon feedstock |
| US20110034647A1 (en) * | 2007-11-29 | 2011-02-10 | Weijian Mo | Systems and methods for making a middle distillate product and lower olefins from a hydrocarbon feedstock |
| US8263008B2 (en) | 2008-12-18 | 2012-09-11 | Uop Llc | Apparatus for improving flow properties of crude petroleum |
| US9157037B2 (en) | 2008-12-18 | 2015-10-13 | Uop Llc | Process for improving flow properties of crude petroleum |
| RU2417246C1 (en) * | 2009-08-03 | 2011-04-27 | Открытое акционерное общество "Славнефть-Ярославнефтеоргсинтез" | Procedure for hydrocarbon stock catalytic cracking |
| 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 |
| JP5876575B2 (en) | 2011-07-29 | 2016-03-02 | サウジ アラビアン オイル カンパニー | Hydrogen rich feedstock for fluid catalytic cracking process |
| CN109297742B (en) * | 2018-11-21 | 2024-03-12 | 上海市计量测试技术研究院 | Catering oil fume generator |
| 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 |
| US4457833A (en) * | 1981-08-27 | 1984-07-03 | Ashland Oil, Inc. | Process and catalyst for the conversion of carbo-metallic containing oils |
| US4508839A (en) * | 1981-08-27 | 1985-04-02 | Ashland Oil, Inc. | 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 DE DE8484112717T patent/DE3473473D1/en not_active Expired
- 1984-12-17 AT AT84112717T patent/ATE36554T1/en not_active IP Right Cessation
- 1984-12-17 EP EP84112717A patent/EP0171460B1/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
Also Published As
| Publication number | Publication date |
|---|---|
| MX165471B (en) | 1992-11-12 |
| CA1265464A (en) | 1990-02-06 |
| RU2091433C1 (en) | 1997-09-27 |
| AU588528B2 (en) | 1989-09-21 |
| JPS614785A (en) | 1986-01-10 |
| AU4311185A (en) | 1985-12-19 |
| DE3473473D1 (en) | 1988-09-22 |
| JPH0226663B2 (en) | 1990-06-12 |
| ATE36554T1 (en) | 1988-09-15 |
| EP0171460A1 (en) | 1986-02-19 |
| EP0171460B1 (en) | 1988-08-17 |
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