JO3013B1 - عملية ووحدة صناعية لتكرير المواد الخام التي تحتوي على مكونات عضوية - Google Patents

عملية ووحدة صناعية لتكرير المواد الخام التي تحتوي على مكونات عضوية

Info

Publication number
JO3013B1
JO3013B1 JOP/2008/0579A JOP20080579A JO3013B1 JO 3013 B1 JO3013 B1 JO 3013B1 JO P20080579 A JOP20080579 A JO P20080579A JO 3013 B1 JO3013 B1 JO 3013B1
Authority
JO
Jordan
Prior art keywords
raw materials
furnace
reactor
solids
containing organic
Prior art date
Application number
JOP/2008/0579A
Other languages
English (en)
Inventor
Andereas Orth Dr
Nikola Anastasijevic Dr
Schneider Gunter
Missalla Michael
Original Assignee
Outotec Oyj
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 Outotec Oyj filed Critical Outotec Oyj
Application granted granted Critical
Publication of JO3013B1 publication Critical patent/JO3013B1/ar

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
    • B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
    • B01J8/18—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles
    • B01J8/1818—Feeding of the fluidising gas
    • 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
    • C10G1/00—Production of liquid hydrocarbon mixtures from oil-shale, oil-sand, or non-melting solid carbonaceous or similar materials, e.g. wood, coal
    • C10G1/02—Production of liquid hydrocarbon mixtures from oil-shale, oil-sand, or non-melting solid carbonaceous or similar materials, e.g. wood, coal by distillation
    • 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
    • B01J2208/00—Processes carried out in the presence of solid particles; Reactors therefor
    • B01J2208/00743—Feeding or discharging of solids
    • B01J2208/00752—Feeding

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Organic Chemistry (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Wood Science & Technology (AREA)
  • General Chemical & Material Sciences (AREA)
  • Combustion & Propulsion (AREA)
  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)

Abstract

يتعلق الاختراع الراهن بعملية تستخدم لتكرير المواد الخام التي تحتوي على مكونات عضوية, مثل المواد الصلبة التي تحتوي على زيت و/أو قار bitumen، وبالتحديد الرمل الزيتي oil sand أو الرمل القيري tar sand أو الطفل الزيتي oil shale, حيث تشمل الخطوات التالية: - تزويد المواد الخام إلى مفاعل وفصل غازات الوقود عند درجة حرارة تتراوح من حوالي 300 إلى 1000 م، يفضل أن تتراوح من حوالي 500 إلى 800 م، - إدخال المواد الصلبة المتبقية في المفاعل التي تتضمن الجزء غير المتبخر من الهيدروكربونات الثقيلة heavy hydrocarbons إلى فرن، - حرق الهيدروكربونات الثقيلة hydrocarbons المتبقية في المواد الصلبة في الفرن عند درجة حرارة تتراوح من 600 إلى 1500 م، يفضل أن تتراوح من 700 إلى 900 م، - إعادة تدوير المواد الصلبة الساخنة من الفرن إلى المفاعل، حيث يـُفصل الجو المؤكسد للفرن عن جو المفاعل بواسطة أداة منع تسريب blocking device
JOP/2008/0579A 2008-02-13 2008-12-24 عملية ووحدة صناعية لتكرير المواد الخام التي تحتوي على مكونات عضوية JO3013B1 (ar)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
DE102008008943.5A DE102008008943B4 (de) 2008-02-13 2008-02-13 Verfahren und Anlage zur Raffination organische Anteile enthaltender Rohstoffe

Publications (1)

Publication Number Publication Date
JO3013B1 true JO3013B1 (ar) 2016-09-05

Family

ID=40791056

Family Applications (1)

Application Number Title Priority Date Filing Date
JOP/2008/0579A JO3013B1 (ar) 2008-02-13 2008-12-24 عملية ووحدة صناعية لتكرير المواد الخام التي تحتوي على مكونات عضوية

Country Status (8)

Country Link
US (2) US8936657B2 (ar)
CN (1) CN101939404B (ar)
BR (1) BRPI0908525A2 (ar)
CA (1) CA2712628C (ar)
DE (1) DE102008008943B4 (ar)
EE (1) EE05631B1 (ar)
JO (1) JO3013B1 (ar)
WO (1) WO2009100840A2 (ar)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
MA53087A (fr) 2018-07-02 2021-06-02 Outotec Finland Oy Dispositif et procédé pour le refroidissement d'un solide à grains fins

Family Cites Families (24)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3093571A (en) * 1958-10-20 1963-06-11 Exxon Research Engineering Co Method and apparatus for treating shale
US3874739A (en) * 1973-08-07 1975-04-01 Exxon Research Engineering Co Method and apparatus for the transfer of entrained solids
CA1081466A (en) * 1976-03-26 1980-07-15 David S. Mitchell Countercurrent plug-like flow of two solids
DE3102819A1 (de) * 1980-01-29 1982-02-18 Babcock-Hitachi K.K., Tokyo Verfahren fuer die rueckgwinnung von waerme bei der kohlevergasung und vorrichtung dafuer
US4507195A (en) 1983-05-16 1985-03-26 Chevron Research Company Coking contaminated oil shale or tar sand oil on retorted solid fines
US5104519A (en) * 1984-11-02 1992-04-14 Mobil Oil Corporation Method and apparatus for removing small catalyst particles in FCC systems
US5059404A (en) * 1989-02-14 1991-10-22 Manufacturing And Technology Conversion International, Inc. Indirectly heated thermochemical reactor apparatus and processes
US4947803A (en) * 1989-05-08 1990-08-14 Hri, Inc. Fludized bed reactor using capped dual-sided contact units and methods for use
US5033413A (en) * 1989-05-08 1991-07-23 Hri, Inc. Fluidized bed combustion system and method utilizing capped dual-sided contact units
US5536488A (en) * 1991-07-01 1996-07-16 Manufacturing And Technology Conversion Indirectly heated thermochemical reactor processes
ES2117039T3 (es) * 1991-10-28 1998-08-01 Tsukishima Kikai Co Procedimiento para fabricar un horno de lecho fluido que tiene un sistema de circulacion exterior.
CA2116745C (en) * 1993-03-03 2007-05-15 Shuichi Nagato Pressurized internal circulating fluidized-bed boiler
CA2095480C (en) * 1993-05-04 1995-02-14 Paulo Goes Koeberle Multistage turbulent circulating fluidized bed reactor
DE19738106C2 (de) 1997-09-01 2001-01-04 Metallgesellschaft Ag Verfahren zum thermischen Behandeln von flüchtige, brennbare Bestandteile enthaltendem Material
US6063263A (en) 1998-04-24 2000-05-16 Uop Llc Process for feed contacting with immediate catalyst separation
US6869521B2 (en) * 2002-04-18 2005-03-22 Uop Llc Process and apparatus for upgrading FCC product with additional reactor with thorough mixing
JP2001241611A (ja) 2000-02-29 2001-09-07 Mitsubishi Heavy Ind Ltd 流動床焼却炉の運転方法とその装置
US20060076275A1 (en) 2002-07-12 2006-04-13 Smith Anthon L Process for the recovery of hydrocarbon fractions from hydrocarbonaceous solids
US20060231459A1 (en) 2005-03-28 2006-10-19 Swan George A Iii FCC process combining molecular separation with staged conversion
US20090118559A1 (en) * 2005-06-06 2009-05-07 Albemarle Netherlands B.V. Oxidic Metal Composition, Its Preparation And Use As Catalyst Composition
US20080202985A1 (en) * 2007-02-23 2008-08-28 Combustion Resources, L.L.C. Method for recovery of hydrocarbon oils from oil shale and other carbonaceous solids
WO2008107929A1 (ja) * 2007-03-02 2008-09-12 Ihi Corporation 循環流動層炉における粒子循環量制御装置
DE102007014435B4 (de) 2007-03-22 2014-03-27 Outotec Oyj Verfahren und Anlage zur Herstellung von Metalloxid aus Metallsalzen
DE102007032683B4 (de) * 2007-07-13 2014-09-11 Outotec Oyj Verfahren und Anlage zur Raffination ölhaltiger Feststoffe

Also Published As

Publication number Publication date
EE05631B1 (et) 2013-02-15
US20150093296A1 (en) 2015-04-02
CA2712628C (en) 2016-04-12
US9764300B2 (en) 2017-09-19
WO2009100840A3 (en) 2010-02-25
CN101939404B (zh) 2015-04-29
BRPI0908525A2 (pt) 2015-09-29
CA2712628A1 (en) 2009-08-20
CN101939404A (zh) 2011-01-05
US8936657B2 (en) 2015-01-20
DE102008008943B4 (de) 2016-10-27
WO2009100840A2 (en) 2009-08-20
DE102008008943A1 (de) 2009-08-27
US20100313475A1 (en) 2010-12-16
EE201000066A (et) 2010-10-15

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