ATE36554T1 - Verfahren zur katalytischen spaltung von residualoelen mit trockengas als auftriebgas in einem steigrohrreaktor. - Google Patents

Verfahren zur katalytischen spaltung von residualoelen mit trockengas als auftriebgas in einem steigrohrreaktor.

Info

Publication number
ATE36554T1
ATE36554T1 AT84112717T AT84112717T ATE36554T1 AT E36554 T1 ATE36554 T1 AT E36554T1 AT 84112717 T AT84112717 T AT 84112717T AT 84112717 T AT84112717 T AT 84112717T AT E36554 T1 ATE36554 T1 AT E36554T1
Authority
AT
Austria
Prior art keywords
gas
catalyst
lift gas
tube reactor
riser tube
Prior art date
Application number
AT84112717T
Other languages
German (de)
English (en)
Inventor
Ronald A Kmecak
William P Hettinger Jr
Stephen M Kovach
Larry M Fraley
Original Assignee
Ashland Oil Inc
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Ashland Oil Inc filed Critical Ashland Oil Inc
Application granted granted Critical
Publication of ATE36554T1 publication Critical patent/ATE36554T1/de

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10GCRACKING 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
    • C10G47/00Cracking of hydrocarbon oils, in the presence of hydrogen or hydrogen- generating compounds, to obtain lower boiling fractions
    • C10G47/24Cracking of hydrocarbon oils, in the presence of hydrogen or hydrogen- generating compounds, to obtain lower boiling fractions with moving solid particles
    • C10G47/30Cracking 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
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10GCRACKING 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
    • C10G11/00Catalytic cracking, in the absence of hydrogen, of hydrocarbon oils
    • C10G11/14Catalytic cracking, in the absence of hydrogen, of hydrocarbon oils with preheated moving solid catalysts
    • C10G11/18Catalytic 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)
AT84112717T 1984-06-13 1984-12-17 Verfahren zur katalytischen spaltung von residualoelen mit trockengas als auftriebgas in einem steigrohrreaktor. ATE36554T1 (de)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
US62019684A 1984-06-13 1984-06-13
EP84112717A EP0171460B1 (en) 1984-06-13 1984-12-17 Residual oil cracking process using dry gas as lift gas initially in riser reactor

Publications (1)

Publication Number Publication Date
ATE36554T1 true ATE36554T1 (de) 1988-09-15

Family

ID=24484979

Family Applications (1)

Application Number Title Priority Date Filing Date
AT84112717T ATE36554T1 (de) 1984-06-13 1984-12-17 Verfahren zur katalytischen spaltung von residualoelen mit trockengas als auftriebgas in einem steigrohrreaktor.

Country Status (9)

Country Link
EP (1) EP0171460B1 (enrdf_load_stackoverflow)
JP (1) JPS614785A (enrdf_load_stackoverflow)
AT (1) ATE36554T1 (enrdf_load_stackoverflow)
AU (1) AU588528B2 (enrdf_load_stackoverflow)
CA (1) CA1265464A (enrdf_load_stackoverflow)
DE (1) DE3473473D1 (enrdf_load_stackoverflow)
IN (1) IN162877B (enrdf_load_stackoverflow)
MX (1) MX165471B (enrdf_load_stackoverflow)
RU (1) RU2091433C1 (enrdf_load_stackoverflow)

Families Citing this family (29)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0662958B2 (ja) * 1985-02-28 1994-08-17 富士スタンダ−ドリサ−チ株式会社 重質油の熱分解法
AU605188B2 (en) * 1986-09-03 1991-01-10 Mobil Oil Corporation Processing of activated heavy hydrocarbon feeds
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
US4802971A (en) * 1986-09-03 1989-02-07 Mobil Oil Corporation Single riser fluidized catalytic cracking process utilizing hydrogen and carbon-hydrogen contributing fragments
US4853105A (en) * 1986-09-03 1989-08-01 Mobil Oil Corporation Multiple riser fluidized catalytic cracking process utilizing hydrogen and carbon-hydrogen contributing fragments
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
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
US4957617A (en) * 1986-09-03 1990-09-18 Mobil Oil Corporation Fluid catalytic cracking
EP0259156A1 (en) * 1986-09-03 1988-03-09 Mobil Oil Corporation Process for fluidized catalytic cracking with reactive fragments
FR2624762B1 (fr) * 1987-12-21 1990-06-08 Total France Procede et dispositif de regeneration de catalyseur en lit fluidise
US5264115A (en) * 1987-12-30 1993-11-23 Compagnie De Raffinage Et De Distribution Total France Process and apparatus for fluidized bed hydrocarbon conversion
FR2625509B1 (fr) * 1987-12-30 1990-06-22 Total France Procede et dispositif de conversion d'hydrocarbures en lit fluidise
FR2628436B1 (fr) * 1988-03-10 1992-04-24 Total France Procede et dispositif de vapocraquage d'hydrocarbures en phase fluidisee de particules caloporteuses
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
EP1046696B1 (en) * 1999-04-23 2014-06-11 China Petrochemical Corporation A catalytic conversion process for producing isobutane and isoparaffin-enriched gasoline
JP4859358B2 (ja) * 2004-09-22 2012-01-25 日揮触媒化成株式会社 接触分解ガソリンの脱硫触媒およびそれを用いた接触分解ガソリンの脱硫方法
CN1986505B (zh) * 2005-12-23 2010-04-14 中国石油化工股份有限公司 一种增产低碳烯烃的催化转化方法
WO2007149921A1 (en) * 2006-06-22 2007-12-27 Shell Oil Company Methods for producing a crude product from selected feed
US20100324232A1 (en) * 2007-10-10 2010-12-23 Weijian Mo Systems and methods for making 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
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
RU2417246C1 (ru) * 2009-08-03 2011-04-27 Открытое акционерное общество "Славнефть-Ярославнефтеоргсинтез" Способ каталитического крекинга углеводородного сырья
FR2953851B1 (fr) * 2009-12-14 2012-12-21 Total Raffinage Marketing Procede de craquage catalytique avec maximisation des bases gazoles
FR2966160B1 (fr) * 2010-10-14 2013-11-15 IFP Energies Nouvelles Procede de craquage catalytique adapte au traitement de charges a faible carbon conradson comportant le recycle d'une coupe cokante selon une technologie nouvelle
US8951406B2 (en) 2011-07-29 2015-02-10 Saudi Arabian Oil Company Hydrogen-enriched feedstock for fluidized catalytic cracking process
CN109297742B (zh) * 2018-11-21 2024-03-12 上海市计量测试技术研究院 餐饮油烟发生器
US11286429B2 (en) * 2020-06-25 2022-03-29 Saudi Arabian Oil Company Process for heavy oil upgrading utilizing hydrogen and water
CN119630626A (zh) * 2022-09-14 2025-03-14 陶氏环球技术有限责任公司 用于利用再生器使烃脱氢的方法

Family Cites Families (9)

* Cited by examiner, † Cited by third party
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

Also Published As

Publication number Publication date
MX165471B (es) 1992-11-12
AU588528B2 (en) 1989-09-21
JPS614785A (ja) 1986-01-10
RU2091433C1 (ru) 1997-09-27
CA1265464A (en) 1990-02-06
IN162877B (enrdf_load_stackoverflow) 1988-07-16
DE3473473D1 (en) 1988-09-22
JPH0226663B2 (enrdf_load_stackoverflow) 1990-06-12
EP0171460B1 (en) 1988-08-17
AU4311185A (en) 1985-12-19
EP0171460A1 (en) 1986-02-19

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Legal Events

Date Code Title Description
UEP Publication of translation of european patent specification
REN Ceased due to non-payment of the annual fee