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ES8106865A1 - Aparato para producir gas de sintesis nh3 a partir de gas decoqueria previamente purificado y su metodo de accionamiento - Google Patents

Aparato para producir gas de sintesis nh3 a partir de gas decoqueria previamente purificado y su metodo de accionamiento

Info

Publication number
ES8106865A1
ES8106865A1 ES496257A ES496257A ES8106865A1 ES 8106865 A1 ES8106865 A1 ES 8106865A1 ES 496257 A ES496257 A ES 496257A ES 496257 A ES496257 A ES 496257A ES 8106865 A1 ES8106865 A1 ES 8106865A1
Authority
ES
Spain
Prior art keywords
gas
coke oven
reaction zone
production
ammonia synthesis
Prior art date
Legal status (The legal status 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 status listed.)
Expired
Application number
ES496257A
Other languages
English (en)
Other versions
ES496257A0 (es
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Didier Engineering GmbH
Original Assignee
Didier Engineering GmbH
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 Didier Engineering GmbH filed Critical Didier Engineering GmbH
Publication of ES8106865A1 publication Critical patent/ES8106865A1/es
Publication of ES496257A0 publication Critical patent/ES496257A0/es
Granted legal-status Critical Current

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
    • B01J8/02—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
    • B01J8/06—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 in tube reactors; the solid particles being arranged in tubes
    • B01J8/062—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 in tube reactors; the solid particles being arranged in tubes being installed in a furnace
    • C—CHEMISTRY; METALLURGY
    • C01—INORGANIC CHEMISTRY
    • C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B3/00—Hydrogen; Gaseous mixtures containing hydrogen; Separation of hydrogen from mixtures containing it; Purification of hydrogen
    • C01B3/02—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen
    • C01B3/025—Preparation or purification of gas mixtures for ammonia synthesis

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Engineering & Computer Science (AREA)
  • Combustion & Propulsion (AREA)
  • Inorganic Chemistry (AREA)
  • Industrial Gases (AREA)
  • Catalysts (AREA)

Abstract

METODO PARA PRODUCIR GAS DE SINTESIS NH3 A PARTIR DE GAS DE COQUERIA PREVIAMENTE PURIFICADO. EL GAS DE PARTIDA SE INTRODUCE EN EL TUBO EXTERIOR (2) POR EL CONDUCTO (4) PASANDO DE ARRIBA ABAJO A TRAVES DEL CATALIZADOR ACTIVO DE NIQUEL COLOCADO EN SU INTERIOR. EL GAS PADA A CONTINUACION AL TUBO INTERIOR (3) QUE CONTIENE UN CATALIZADOR MENOS ACTIVO SOBRE BASE DE AL2O3 SALIENDO POR EL CONDUCTO (5). EL REACTOR DE DOBLE TUBO (1) SE MANTIENE EN EL INTERIOR DE UN HORNO DE REACCION (7) A UNA TEMPERATURA DE 500 GC. LA PRESION EN EL INTERIOR DE LOS TUBOS ES DE 1 BAR A 40 BAR.
ES496257A 1979-11-29 1980-10-24 Aparato para producir gas de sintesis nh3 a partir de gas decoqueria previamente purificado y su metodo de accionamiento Granted ES496257A0 (es)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
DE19792948107 DE2948107A1 (de) 1979-11-29 1979-11-29 Vorrichtung zur erzeugung von nh (pfeil abwaerts)3(pfeil abwaerts) -synthesegas aus vorgereinigtem kokereigas

Publications (2)

Publication Number Publication Date
ES8106865A1 true ES8106865A1 (es) 1981-10-01
ES496257A0 ES496257A0 (es) 1981-10-01

Family

ID=6087203

Family Applications (1)

Application Number Title Priority Date Filing Date
ES496257A Granted ES496257A0 (es) 1979-11-29 1980-10-24 Aparato para producir gas de sintesis nh3 a partir de gas decoqueria previamente purificado y su metodo de accionamiento

Country Status (4)

Country Link
US (1) US4336229A (es)
DE (1) DE2948107A1 (es)
ES (1) ES496257A0 (es)
ZA (1) ZA807353B (es)

Families Citing this family (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE3100641C2 (de) * 1981-01-12 1985-08-01 Didier Engineering Gmbh, 4300 Essen Verfahren zum Betreiben einer Vorrichtung zur Erzeugung von Spaltgas für die Herstellung von NH↓3↓-Synthesegas
EP0287238B1 (en) * 1987-04-13 1991-09-11 Imperial Chemical Industries Plc Process and apparatus for the production of a hot pressurised gas stream by catalytic combustion
FR2614612B1 (fr) * 1987-04-28 1990-09-14 Technip Cie Procede de production amelioree de gaz d'ammoniac et installation pour l'execution de ce procede
DE3942207C2 (de) * 1989-12-21 1999-09-30 Diatest Hermann Koeltgen Gmbh Bohrungsmeßgerät
US5413773A (en) * 1990-10-09 1995-05-09 General Motors Corporation Method for forming carbon filters
US5024818A (en) * 1990-10-09 1991-06-18 General Motors Corporation Apparatus for forming carbon fibers
DE4327176C1 (de) * 1993-08-13 1995-01-26 Metallgesellschaft Ag Röhrenofen für die Erzeugung kohlenmonoxidhaltiger Gasgemische
US5552131A (en) * 1994-06-30 1996-09-03 Arco Chemical Technology, L.P. Oxidation of secondary alcohols
BR112022003964A2 (pt) * 2019-09-03 2022-05-24 Haldor Topsoe As Forno reformador com tubos reformadores suportados

Family Cites Families (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US1826548A (en) * 1926-07-24 1931-10-06 Selden Co Catalytic apparatus
US2013652A (en) * 1931-06-04 1935-09-10 Ici Ltd Method for the production of nitrogen and hydrogen by the thermal decomposition of ammonia
US3450507A (en) * 1966-10-27 1969-06-17 Chemical Construction Corp Integrated reforming of hydrocarbons
US3544264A (en) * 1968-09-25 1970-12-01 Universal Oil Prod Co Method and means for two-stage catalytic treating of engine exhaust gases
US3607125A (en) * 1968-12-30 1971-09-21 Gen Electric Reformer tube construction
DE2705324A1 (de) * 1977-02-09 1978-08-10 Ght Hochtemperaturreak Tech Spaltrohrofen

Also Published As

Publication number Publication date
US4336229A (en) 1982-06-22
ZA807353B (en) 1981-11-25
ES496257A0 (es) 1981-10-01
DE2948107A1 (de) 1981-06-04

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