BRPI0412200A - método de controlar a temperatura de uma reação exotérmica - Google Patents

método de controlar a temperatura de uma reação exotérmica

Info

Publication number
BRPI0412200A
BRPI0412200A BRPI0412200-3A BRPI0412200A BRPI0412200A BR PI0412200 A BRPI0412200 A BR PI0412200A BR PI0412200 A BRPI0412200 A BR PI0412200A BR PI0412200 A BRPI0412200 A BR PI0412200A
Authority
BR
Brazil
Prior art keywords
temperature
exothermic reaction
controlling
reactor
vapor phase
Prior art date
Application number
BRPI0412200-3A
Other languages
English (en)
Inventor
Dennis J O'rear
Charles L Kibby
Original Assignee
Chevron Usa 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 Chevron Usa Inc filed Critical Chevron Usa Inc
Publication of BRPI0412200A publication Critical patent/BRPI0412200A/pt

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
    • C10G2/00—Production of liquid hydrocarbon mixtures of undefined composition from oxides of carbon
    • C10G2/30—Production of liquid hydrocarbon mixtures of undefined composition from oxides of carbon from carbon monoxide with hydrogen
    • C10G2/32—Production of liquid hydrocarbon mixtures of undefined composition from oxides of carbon from carbon monoxide with hydrogen with the use of catalysts
    • C10G2/34—Apparatus, reactors
    • C10G2/342—Apparatus, reactors with moving solid catalysts
    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C27/00—Processes involving the simultaneous production of more than one class of oxygen-containing compounds
    • 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
    • B01J8/20—Chemical 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
    • B01J8/22—Chemical 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
    • 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
    • B01J2208/00008—Controlling the process
    • B01J2208/00017—Controlling the temperature
    • B01J2208/00026—Controlling or regulating the heat exchange system
    • B01J2208/00035—Controlling or regulating the heat exchange system involving measured parameters
    • B01J2208/00044—Temperature measurement
    • B01J2208/00061—Temperature measurement of the reactants
    • 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
    • B01J2208/00008—Controlling the process
    • B01J2208/00017—Controlling the temperature
    • B01J2208/00106—Controlling the temperature by indirect heat exchange
    • B01J2208/00168—Controlling the temperature by indirect heat exchange with heat exchange elements outside the bed of solid particles
    • B01J2208/00256—Controlling the temperature by indirect heat exchange with heat exchange elements outside the bed of solid particles in a heat exchanger for the heat exchange medium separate from the reactor
    • 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
    • B01J2208/00008—Controlling the process
    • B01J2208/00017—Controlling the temperature
    • B01J2208/00106—Controlling the temperature by indirect heat exchange
    • B01J2208/00265—Part of all of the reactants being heated or cooled outside the reactor while recycling
    • B01J2208/00274—Part of all of the reactants being heated or cooled outside the reactor while recycling involving reactant vapours

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • General Chemical & Material Sciences (AREA)
  • Combustion & Propulsion (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
  • Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)
  • Physical Or Chemical Processes And Apparatus (AREA)
  • Devices And Processes Conducted In The Presence Of Fluids And Solid Particles (AREA)

Abstract

"MéTODO DE CONTROLAR A TEMPERATURA DE UMA REAçãO EXOTéRMICA". Novos métodos de controlar a temperatura de uma reação exotérmica são divulgados. Tais métodos são particularmente aplicáveis a uma reação de síntese de Fischer-Tropsch e compreende remover um produto da fase vapor do reator de Fischer-Tropsch, condensando pelo menos uma porção do produto da fase vapor para formar um líquido volatilizável e injetando pelo menos uma porção do líquido volatilizável no reator, em que o líquido volatilizável compreende hidrocarbonetos que estão na faixa de ponto de ebulição mais alta do produto da fase vapor que é removido do reator.
BRPI0412200-3A 2003-07-02 2004-07-02 método de controlar a temperatura de uma reação exotérmica BRPI0412200A (pt)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
US10/613,594 US6822006B1 (en) 2003-07-02 2003-07-02 Methods of controlling the temperature of an exothermic reaction
PCT/US2004/021443 WO2005003702A2 (en) 2003-07-02 2004-07-02 Methods of controlling the temperature of an exothermic reaction

Publications (1)

Publication Number Publication Date
BRPI0412200A true BRPI0412200A (pt) 2006-08-22

Family

ID=33435477

Family Applications (1)

Application Number Title Priority Date Filing Date
BRPI0412200-3A BRPI0412200A (pt) 2003-07-02 2004-07-02 método de controlar a temperatura de uma reação exotérmica

Country Status (8)

Country Link
US (1) US6822006B1 (pt)
JP (1) JP4768610B2 (pt)
AU (1) AU2004254637A1 (pt)
BR (1) BRPI0412200A (pt)
GB (1) GB2421201B (pt)
NL (1) NL1026568C2 (pt)
WO (1) WO2005003702A2 (pt)
ZA (1) ZA200600305B (pt)

Families Citing this family (14)

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Publication number Priority date Publication date Assignee Title
GB2382786B (en) * 2001-12-04 2005-10-19 Sasol Technology Slurry phase apparatus
DE102005056784A1 (de) * 2005-11-28 2007-05-31 Basf Ag Verfahren zur Herstellung von Olefinen aus Synthesegas in einer Reaktionskolonne
JP2007277465A (ja) * 2006-04-10 2007-10-25 Nippon Oil Corp 一酸化炭素の還元による炭化水素の製造方法
JP5277364B2 (ja) * 2007-03-30 2013-08-28 公益財団法人北九州産業学術推進機構 一酸化炭素の還元による炭化水素の製造方法
JP2008277696A (ja) * 2007-05-07 2008-11-13 Toshiba Corp 半導体装置の製造方法
EP2199368B8 (en) * 2007-09-27 2013-09-11 Nippon Steel & Sumikin Engineering Co., Ltd. Bubble-column-type hydrocarbon synthesis reactor, and hydrocarbon synthesis reaction system having the reactor
US20090249682A1 (en) * 2008-04-07 2009-10-08 Gunnerman Rudolf W Conversion of biogas to liquid fuels
NZ593430A (en) * 2008-12-15 2012-11-30 Sasol Tech Pty Ltd Process for regenerating spent cobalt Fischer Tropsch synthesis catalysts
JP5675146B2 (ja) 2010-03-30 2015-02-25 独立行政法人石油天然ガス・金属鉱物資源機構 炭化水素の製造方法
JP5950500B2 (ja) * 2011-03-17 2016-07-13 独立行政法人石油天然ガス・金属鉱物資源機構 炭化水素の製造装置及び炭化水素の製造方法
US20140021094A1 (en) * 2011-03-31 2014-01-23 Japan Oil, Gas And Metals National Corporation Method of removing heavy hydrocarbons
GB201206196D0 (en) * 2012-04-05 2012-05-23 Ingengtl Production of liquid hydrocarbons
CN103962071B (zh) * 2013-02-05 2018-01-30 上海碧科清洁能源技术有限公司 浆态床反应设备及其使用方法
US11377598B2 (en) 2018-05-11 2022-07-05 Sabic Global Technologies B.V. Method related to heat transfer for exothermic reactions

Family Cites Families (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2438029A (en) 1944-05-03 1948-03-16 Texas Co Method of effecting catalytic conversions
NL8101447A (nl) 1981-03-24 1982-10-18 Shell Int Research Werkwijze voor de bereiding van koolwaterstoffen uit koolstofhoudend materiaal.
US5252613A (en) 1992-12-18 1993-10-12 Exxon Research & Engineering Company Enhanced catalyst mixing in slurry bubble columns (OP-3723)
FR2741064B1 (fr) * 1995-11-10 1997-12-12 Inst Francais Du Petrole Procede de conversion de gaz de synthese en hydrocarbures
US5856606A (en) * 1996-09-27 1999-01-05 Uop Llc Turbulent bed solid catalyst hydrocarbon alkylation process
JPH10192690A (ja) * 1996-12-27 1998-07-28 Nkk Corp スラリー床反応器
US6160026A (en) 1997-09-24 2000-12-12 Texaco Inc. Process for optimizing hydrocarbon synthesis
RU2156650C1 (ru) 1998-12-30 2000-09-27 Институт катализа им. Г.К.Борескова СО РАН Способ осуществления процесса синтеза фишера-тропша (варианты) и способ выбора стационарного состава растворителя в сларри реакторе
AU9397801A (en) 2000-10-13 2002-04-22 Bp Exploration Operating Fischer-tropsch synthesis process
US6590002B2 (en) 2001-07-13 2003-07-08 Exxonmobil Research And Engineering Company Temperature controlled in situ wax purification
JP3717455B2 (ja) * 2002-03-13 2005-11-16 独立行政法人科学技術振興機構 フィッシャー・トロプシュ法による炭化水素の製造方法とその触媒

Also Published As

Publication number Publication date
JP4768610B2 (ja) 2011-09-07
WO2005003702A2 (en) 2005-01-13
GB0600808D0 (en) 2006-02-22
ZA200600305B (en) 2007-05-30
AU2004254637A1 (en) 2005-01-13
NL1026568C2 (nl) 2005-12-14
WO2005003702A3 (en) 2005-03-10
GB2421201B (en) 2007-07-25
NL1026568A1 (nl) 2005-01-04
JP2007530709A (ja) 2007-11-01
US6822006B1 (en) 2004-11-23
GB2421201A (en) 2006-06-21

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Legal Events

Date Code Title Description
B08F Application dismissed because of non-payment of annual fees [chapter 8.6 patent gazette]

Free format text: REFERENTE AS 7A E 8A ANUIDADES.

B08K Patent lapsed as no evidence of payment of the annual fee has been furnished to inpi [chapter 8.11 patent gazette]

Free format text: REFERENTE AO DESPACHO 8.6 PUBLICADO NA RPI 2159 DE 22/05/2012.