NO990881L - Boblekolonnereaktor med suger°r og fremgangsmÕte for regenerering av katalysatoren inneholdt deri - Google Patents

Boblekolonnereaktor med suger°r og fremgangsmÕte for regenerering av katalysatoren inneholdt deri

Info

Publication number
NO990881L
NO990881L NO990881A NO990881A NO990881L NO 990881 L NO990881 L NO 990881L NO 990881 A NO990881 A NO 990881A NO 990881 A NO990881 A NO 990881A NO 990881 L NO990881 L NO 990881L
Authority
NO
Norway
Prior art keywords
suction tube
regeneration process
bubble column
column reactor
catalyst regeneration
Prior art date
Application number
NO990881A
Other languages
English (en)
Other versions
NO318137B1 (no
NO990881D0 (no
Inventor
Cristina Maretto
Vincenzo Piccolo
Dominique Casanave
Pierre Galtier
Original Assignee
Agip Petroli
Eni Spa
Inst Francais Du Petrole
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 Agip Petroli, Eni Spa, Inst Francais Du Petrole filed Critical Agip Petroli
Publication of NO990881D0 publication Critical patent/NO990881D0/no
Publication of NO990881L publication Critical patent/NO990881L/no
Publication of NO318137B1 publication Critical patent/NO318137B1/no

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
    • C10G2/00Production of liquid hydrocarbon mixtures of undefined composition from oxides of carbon
    • C10G2/30Production of liquid hydrocarbon mixtures of undefined composition from oxides of carbon from carbon monoxide with hydrogen
    • C10G2/32Production of liquid hydrocarbon mixtures of undefined composition from oxides of carbon from carbon monoxide with hydrogen with the use of catalysts
    • C10G2/34Apparatus, reactors
    • C10G2/342Apparatus, reactors with moving solid catalysts
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J38/00Regeneration or reactivation of catalysts, in general
    • B01J38/48Liquid treating or treating in liquid phase, e.g. dissolved or suspended
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J8/00Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
    • B01J8/18Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles
    • B01J8/20Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles with liquid as a fluidising medium
    • B01J8/22Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles with liquid as a fluidising medium gas being introduced into the liquid
    • B01J8/224Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles with liquid as a fluidising medium gas being introduced into the liquid the particles being subject to a circulatory movement
    • B01J8/226Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles with liquid as a fluidising medium gas being introduced into the liquid the particles being subject to a circulatory movement internally, i.e. the particles rotate within the vessel
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C1/00Preparation of hydrocarbons from one or more compounds, none of them being a hydrocarbon
    • C07C1/02Preparation of hydrocarbons from one or more compounds, none of them being a hydrocarbon from oxides of a carbon
    • C07C1/04Preparation of hydrocarbons from one or more compounds, none of them being a hydrocarbon from oxides of a carbon from carbon monoxide with hydrogen
    • C07C1/0485Set-up of reactors or accessories; Multi-step processes
    • C07C1/049Coupling of the reaction and regeneration of the catalyst
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2208/00Processes carried out in the presence of solid particles; Reactors therefor
    • B01J2208/00008Controlling the process
    • B01J2208/00017Controlling the temperature
    • B01J2208/00106Controlling the temperature by indirect heat exchange
    • B01J2208/00115Controlling the temperature by indirect heat exchange with heat exchange elements inside the bed of solid particles
    • B01J2208/00132Tubes
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2208/00Processes carried out in the presence of solid particles; Reactors therefor
    • B01J2208/00796Details of the reactor or of the particulate material
    • B01J2208/00823Mixing elements
    • B01J2208/00831Stationary elements
    • B01J2208/0084Stationary elements inside the bed, e.g. baffles
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2219/00Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J2219/00002Chemical plants
    • B01J2219/00027Process aspects
    • B01J2219/00033Continuous processes
    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P20/00Technologies relating to chemical industry
    • Y02P20/50Improvements relating to the production of bulk chemicals
    • Y02P20/584Recycling of catalysts

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Engineering & Computer Science (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • General Chemical & Material Sciences (AREA)
  • Materials Engineering (AREA)
  • Combustion & Propulsion (AREA)
  • Devices And Processes Conducted In The Presence Of Fluids And Solid Particles (AREA)
  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Catalysts (AREA)
NO19990881A 1997-06-26 1999-02-24 Fremgangsmate for regenerering i en boblekolonnereaktor med sugeror av katalysatoren inneholdt deri. NO318137B1 (no)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
IT97MI001509A IT1292422B1 (it) 1997-06-26 1997-06-26 Reattore a bolle con draft tube e procedimento per la rigenerazione del catalizzatore in esso contenuto
PCT/EP1998/003874 WO1999000191A2 (en) 1997-06-26 1998-06-20 Bubble-column reactor with draft-tube and process for the regeneration of the catalyst contained therein

Publications (3)

Publication Number Publication Date
NO990881D0 NO990881D0 (no) 1999-02-24
NO990881L true NO990881L (no) 1999-04-26
NO318137B1 NO318137B1 (no) 2005-02-07

Family

ID=11377442

Family Applications (1)

Application Number Title Priority Date Filing Date
NO19990881A NO318137B1 (no) 1997-06-26 1999-02-24 Fremgangsmate for regenerering i en boblekolonnereaktor med sugeror av katalysatoren inneholdt deri.

Country Status (14)

Country Link
US (1) US6162754A (no)
EP (1) EP0923413B1 (no)
JP (1) JP4083819B2 (no)
CN (1) CN1163455C (no)
CA (1) CA2264572C (no)
DE (1) DE69816576T2 (no)
ES (1) ES2205529T3 (no)
ID (1) ID21080A (no)
IT (1) IT1292422B1 (no)
MY (1) MY120749A (no)
NO (1) NO318137B1 (no)
RU (1) RU2198868C2 (no)
SA (1) SA98190950B1 (no)
WO (1) WO1999000191A2 (no)

Families Citing this family (24)

* Cited by examiner, † Cited by third party
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FR2751227B1 (fr) * 1996-07-19 1998-11-27 Rhone Merieux Formule de vaccin polynucleotidique contre les pathologies canines, notamment les pathologies respiratoires et digestives
US6323248B1 (en) * 2000-06-02 2001-11-27 Exxonmobil Research And Engineering Company Slurry hydrocarbon synthesis with fresh catalyst activity increase during hydrocarbon production
US20020143075A1 (en) * 2001-03-27 2002-10-03 Agee Kenneth L. Low-profile moving bed reactor
US20040000474A1 (en) * 2002-02-22 2004-01-01 Catalytic Distillation Technologies Liquid-continuous column distillation
US6838487B1 (en) 2003-12-04 2005-01-04 Rentech, Inc. Method and apparatus for regenerating an iron-based Fischer-Tropsch catalyst
CN101094717A (zh) * 2004-12-31 2007-12-26 国际壳牌研究有限公司 用于固/液/气反应的反应器
RU2391132C2 (ru) * 2005-03-17 2010-06-10 Сэсол Текнолоджи (Проприетери) Лимитед Реактор с псевдоожиженным слоем, трехфазный шламовый реактор и способы обеспечения их функционирования (варианты)
JP2007197636A (ja) * 2006-01-30 2007-08-09 Nippon Steel Engineering Co Ltd 気泡塔型炭化水素合成反応器
US7666366B2 (en) 2006-07-10 2010-02-23 Exxonmobil Chemical Patents Inc. Internal loop reactor and Oxo process using same
CN101505867A (zh) * 2006-08-25 2009-08-12 新日铁工程技术株式会社 从合成气体制造烃的催化剂、催化剂的制造方法、催化剂的再生方法以及从合成气体制造烃的方法
WO2008139407A2 (en) * 2007-05-11 2008-11-20 Sasol Technology (Proprietary) Limited Catalysts
CN101809123B (zh) * 2007-08-10 2014-04-30 Sasol技术股份有限公司 烃合成方法
US8614158B2 (en) * 2008-02-29 2013-12-24 Schlumberger Technology Corporation Fischer-trospch and oxygenate synthesis catalyst activation/regeneration in a micro scale process
US8293805B2 (en) * 2008-05-29 2012-10-23 Schlumberger Technology Corporation Tracking feedstock production with micro scale gas-to-liquid units
EA021337B1 (ru) * 2008-09-30 2015-05-29 Джэпэн Ойл, Гэз Энд Металз Нэшнл Корпорейшн Реактор в виде барботажной колонны и способ управления реактором в виде барботажной колонны
US8680162B2 (en) * 2008-12-15 2014-03-25 Sasol Technology (Proprietary) Limited Catalysts
EP2367630A1 (en) * 2008-12-18 2011-09-28 Shell Internationale Research Maatschappij B.V. Regeneration of a fischer tropsch catalyst by oxidating it and treating it with a mixture of ammonium carbonate, ammonium hydroxide and water
US8497310B2 (en) 2008-12-22 2013-07-30 Shell Oil Company Integrated process and reactor arrangement for hydrocarbon synthesis
US20100303683A1 (en) * 2009-05-04 2010-12-02 Kelvin John Hendrie Cooling module and reactor comprising the same
JP2014136767A (ja) * 2013-01-17 2014-07-28 Japan Oil Gas & Metals National Corp 炭化水素合成反応装置
WO2015025225A2 (en) * 2013-08-21 2015-02-26 Saudi Basic Industries Corporation A process for the production of hydrocarbons
JP6518480B2 (ja) * 2015-03-30 2019-05-22 株式会社クボタ 気泡塔型スラリー床反応装置
RU204762U1 (ru) * 2019-07-19 2021-06-09 Федеральное государственное бюджетное учреждение науки Ордена Трудового Красного Знамени Институт нефтехимического синтеза им. А.В. Топчиева Российской академии наук (ИНХС РАН) Устройство для проведения реакций в суспензионном слое наноразмерного катализатора
RU195804U1 (ru) * 2019-07-19 2020-02-05 Федеральное государственное бюджетное учреждение науки Ордена Трудового Красного Знамени Институт нефтехимического синтеза им. А. В. Топчиева Российской академии наук (ИНХС РАН) Устройство для проведения каталитических процессов в трехфазном суспензионном слое

Family Cites Families (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS501700B1 (no) * 1969-06-21 1975-01-21
EP0325337B1 (en) * 1988-01-20 1993-08-25 Paques B.V. Process for reducing the hysteresis effect in a gaslift loop reactor with suspended solid particles
US5292705A (en) * 1992-09-24 1994-03-08 Exxon Research & Engineering Co. Activation of hydrocarbon synthesis catalyst
US5252613A (en) * 1992-12-18 1993-10-12 Exxon Research & Engineering Company Enhanced catalyst mixing in slurry bubble columns (OP-3723)
US5268344A (en) * 1992-12-18 1993-12-07 Exxon Research & Engineering Company Draft tube for catalyst rejuvenation and distribution
US5288673A (en) * 1992-12-18 1994-02-22 Exxon Research And Engineering Company Temperature control in draft tubes for catalyst rejuvenation
FR2751564B1 (fr) * 1996-07-26 2001-10-12 Inst Francais Du Petrole Procede et dispositif pour le fonctionnement d'une colonne a bulles triphasique avec application en synthese fischer-tropsch
IT1283774B1 (it) * 1996-08-07 1998-04-30 Agip Petroli Processo di fischer-tropsch con reattore a colonna a bolle multistadio

Also Published As

Publication number Publication date
SA98190950B1 (ar) 2006-05-01
WO1999000191A2 (en) 1999-01-07
RU2198868C2 (ru) 2003-02-20
WO1999000191A3 (en) 1999-03-25
CN1230941A (zh) 1999-10-06
JP4083819B2 (ja) 2008-04-30
JP2000516966A (ja) 2000-12-19
EP0923413B1 (en) 2003-07-23
ID21080A (id) 1999-04-15
DE69816576D1 (de) 2003-08-28
US6162754A (en) 2000-12-19
MY120749A (en) 2005-11-30
IT1292422B1 (it) 1999-02-08
CA2264572A1 (en) 1999-01-07
ITMI971509A0 (no) 1997-06-26
CN1163455C (zh) 2004-08-25
NO318137B1 (no) 2005-02-07
DE69816576T2 (de) 2004-05-13
CA2264572C (en) 2007-05-29
ITMI971509A1 (it) 1998-12-26
EP0923413A2 (en) 1999-06-23
ES2205529T3 (es) 2004-05-01
NO990881D0 (no) 1999-02-24

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