BR9810493A - Método para ignição de uma reação de fase gasosa catalisada - Google Patents

Método para ignição de uma reação de fase gasosa catalisada

Info

Publication number
BR9810493A
BR9810493A BR9810493-4A BR9810493A BR9810493A BR 9810493 A BR9810493 A BR 9810493A BR 9810493 A BR9810493 A BR 9810493A BR 9810493 A BR9810493 A BR 9810493A
Authority
BR
Brazil
Prior art keywords
reactor
gas phase
ignition
reaction
chemical reaction
Prior art date
Application number
BR9810493-4A
Other languages
English (en)
Inventor
Theodore A Koch
Mehrdad Mehdizadeh
David Julian Bueker
Original Assignee
Du Pont
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 Du Pont filed Critical Du Pont
Publication of BR9810493A publication Critical patent/BR9810493A/pt

Links

Classifications

    • C—CHEMISTRY; METALLURGY
    • C01—INORGANIC CHEMISTRY
    • C01C—AMMONIA; CYANOGEN; COMPOUNDS THEREOF
    • C01C3/00—Cyanogen; Compounds thereof
    • C01C3/02—Preparation, separation or purification of hydrogen cyanide
    • C01C3/0208—Preparation in gaseous phase
    • C01C3/0212—Preparation in gaseous phase from hydrocarbons and ammonia in the presence of oxygen, e.g. the Andrussow-process
    • C01C3/022—Apparatus therefor
    • C01C3/0225—Apparatus therefor characterised by the synthesis 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
    • B01J12/00—Chemical processes in general for reacting gaseous media with gaseous media; Apparatus specially adapted therefor
    • B01J12/007—Chemical processes in general for reacting gaseous media with gaseous media; Apparatus specially adapted therefor in the presence of catalytically active bodies, e.g. porous plates
    • 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
    • B01J19/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J19/08—Processes employing the direct application of electric or wave energy, or particle radiation; Apparatus therefor
    • B01J19/087—Processes employing the direct application of electric or wave energy, or particle radiation; Apparatus therefor employing electric or magnetic energy
    • 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
    • B01J8/02—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds
    • B01J8/0285—Heating or cooling the reactor
    • C—CHEMISTRY; METALLURGY
    • C01—INORGANIC CHEMISTRY
    • C01C—AMMONIA; CYANOGEN; COMPOUNDS THEREOF
    • C01C3/00—Cyanogen; Compounds thereof
    • C01C3/02—Preparation, separation or purification of hydrogen cyanide
    • C01C3/0208—Preparation in gaseous phase
    • C01C3/0212—Preparation in gaseous phase from hydrocarbons and ammonia in the presence of oxygen, e.g. the Andrussow-process
    • 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
    • B01J2208/00389—Controlling the temperature using electric heating or cooling elements
    • B01J2208/00398—Controlling the temperature using electric heating or cooling elements inside the reactor bed
    • 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
    • B01J2208/00389—Controlling the temperature using electric heating or cooling elements
    • B01J2208/00407—Controlling the temperature using electric heating or cooling elements outside the reactor bed
    • 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
    • B01J2208/00389—Controlling the temperature using electric heating or cooling elements
    • B01J2208/00415—Controlling the temperature using electric heating or cooling elements electric resistance heaters
    • 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
    • B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J2219/19—Details relating to the geometry of the reactor
    • B01J2219/194—Details relating to the geometry of the reactor round
    • B01J2219/1941—Details relating to the geometry of the reactor round circular or disk-shaped
    • B01J2219/1946—Details relating to the geometry of the reactor round circular or disk-shaped conical
    • 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
    • B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J2219/32—Details relating to packing elements in the form of grids or built-up elements for forming a unit of module inside the apparatus for mass or heat transfer
    • B01J2219/324—Composition or microstructure of the elements
    • B01J2219/32466—Composition or microstructure of the elements comprising catalytically active material

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Health & Medical Sciences (AREA)
  • General Health & Medical Sciences (AREA)
  • Toxicology (AREA)
  • Inorganic Chemistry (AREA)
  • Physical Or Chemical Processes And Apparatus (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Devices And Processes Conducted In The Presence Of Fluids And Solid Particles (AREA)

Abstract

<B>"MéTODO PARA IGNIçãO DE UMA REAçãO DE FASE GASOSA CATALISADA"<D> A presente invenção trata-se de um método aperfeiçoado de ignição de uma reação química de fase gasosa catalisada, o qual envolve o ato de se empregar um vaso do reator (10), sendo que o reagente gasoso, atravessando continuamente o reator, entra em contato com um meio catalisador metálico de fase sólida (18), com uma bobina indutiva (14) dentro do reator (10) no lado de entrada do catalisador, e uma barreira contra faísca e radiação térmica e porosa (17) entre a bobina de indução (14) e o catalisador sólido (18). De acordo com o método aperfeiçoado de ignição, o meio catalisador metálico (18) é indutivamente aquecido a fim de iniciar a ignição da reação química, e depois da ignição o aquecimento indutivo é suspenso e se baseia na exotermia da reação química para sustentar a temperatura da reação. Esse reator e método de operação é particularmente útil para a produção contínua de cianeto de hidrogênio pelo processo de Andrussow.
BR9810493-4A 1997-07-03 1998-07-02 Método para ignição de uma reação de fase gasosa catalisada BR9810493A (pt)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
US5165997P 1997-07-03 1997-07-03
PCT/US1998/013825 WO1999001211A1 (en) 1997-07-03 1998-07-02 Method of inductively igniting a chemical reaction

Publications (1)

Publication Number Publication Date
BR9810493A true BR9810493A (pt) 2000-09-12

Family

ID=21972629

Family Applications (1)

Application Number Title Priority Date Filing Date
BR9810493-4A BR9810493A (pt) 1997-07-03 1998-07-02 Método para ignição de uma reação de fase gasosa catalisada

Country Status (13)

Country Link
EP (1) EP1001843B1 (pt)
JP (1) JP4001931B2 (pt)
KR (1) KR100474613B1 (pt)
CN (1) CN1112962C (pt)
AU (1) AU727003B2 (pt)
BR (1) BR9810493A (pt)
CA (1) CA2291771A1 (pt)
DE (1) DE69805079T2 (pt)
ID (1) ID24281A (pt)
PL (1) PL337796A1 (pt)
RU (1) RU2193918C2 (pt)
SK (1) SK283767B6 (pt)
WO (1) WO1999001211A1 (pt)

Families Citing this family (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
AU2603902A (en) * 2000-12-05 2002-06-18 Texaco Development Corp Apparatus and method for heating catalyst for start-up of a compact fuel processor
EP1419812B1 (en) * 2002-11-15 2015-09-16 Haldor Topsoe A/S High temperature fixed bed reactor and its use
CN1931421B (zh) * 2005-09-16 2011-04-27 亚申科技研发中心（上海）有限公司 反应系统
DE102007034715A1 (de) * 2007-07-23 2009-01-29 Evonik Röhm Gmbh Reaktor zur Herstellung von Cyanwasserstoff nach dem Andrussow-Verfahren
FR3008626B1 (fr) * 2013-07-19 2015-08-07 Arkema France Reacteur pour preparer du cyanure d'hydrogene par le procede d'andrussow, equipement comprenant ledit reacteur et procede utilisant un tel equipement
EP3448804B1 (en) * 2016-04-26 2021-08-18 Haldor Topsøe A/S A process for producing hydrogen or syngas by methanol cracking
TWI774668B (zh) * 2016-04-26 2022-08-21 丹麥商托普索公司 用於氨合成轉換器之起動加熱的方法

Family Cites Families (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2443423A (en) * 1946-04-29 1948-06-15 Phillips Petroleum Co Apparatus for conducting endothermic catalytic conversions
GB729502A (en) * 1951-12-06 1955-05-04 Goodrich Co B F Improvements in or relating to a process for the production of hydrogen cyanide
GB854268A (en) * 1956-02-25 1960-11-16 Shawinigan Chem Ltd The electrothermic production of hydrogen cyanide by fluidized bed techniques
US3215495A (en) * 1962-01-23 1965-11-02 Du Pont Apparatus and process for preparing hydrogen cyanide
DE4209195A1 (de) * 1992-03-18 1993-09-23 Mannesmann Ag Katalysator fuer heterogene katalyse
JP3377617B2 (ja) * 1994-09-07 2003-02-17 電気興業株式会社 排気ガス浄化装置
DE4444366A1 (de) * 1994-12-14 1996-06-20 Chemtec Leuna Ges Fuer Chemie Verfahren zur kontinuierlichen Durchführung exothermer Reaktionen in einem Festbettreaktor

Also Published As

Publication number Publication date
JP4001931B2 (ja) 2007-10-31
PL337796A1 (en) 2000-09-11
DE69805079D1 (de) 2002-05-29
DE69805079T2 (de) 2002-11-07
KR100474613B1 (ko) 2005-03-08
RU2193918C2 (ru) 2002-12-10
EP1001843B1 (en) 2002-04-24
WO1999001211A1 (en) 1999-01-14
CA2291771A1 (en) 1999-01-14
KR20010014421A (ko) 2001-02-26
CN1112962C (zh) 2003-07-02
ID24281A (id) 2000-07-13
SK173399A3 (en) 2001-03-12
AU8285098A (en) 1999-01-25
SK283767B6 (sk) 2004-01-08
AU727003B2 (en) 2000-11-30
CN1261822A (zh) 2000-08-02
JP2002507936A (ja) 2002-03-12
EP1001843A1 (en) 2000-05-24

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Owner name: INVISTA TECHNOLOGIES S.A.R.L. (US)

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