IL28758A - Reactor for the continuous performance of exothermic catalyzed reactions in the gas phase under high pressure - Google Patents

Reactor for the continuous performance of exothermic catalyzed reactions in the gas phase under high pressure

Info

Publication number
IL28758A
IL28758A IL28758A IL2875867A IL28758A IL 28758 A IL28758 A IL 28758A IL 28758 A IL28758 A IL 28758A IL 2875867 A IL2875867 A IL 2875867A IL 28758 A IL28758 A IL 28758A
Authority
IL
Israel
Prior art keywords
catalyst
heat exchanger
heat
reactor
gas
Prior art date
Application number
IL28758A
Other languages
English (en)
Original Assignee
Montedison Spa
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 Montedison Spa filed Critical Montedison Spa
Publication of IL28758A publication Critical patent/IL28758A/en

Links

Classifications

    • C—CHEMISTRY; METALLURGY
    • C01—INORGANIC CHEMISTRY
    • C01C—AMMONIA; CYANOGEN; COMPOUNDS THEREOF
    • C01C1/00—Ammonia; Compounds thereof
    • C01C1/02—Preparation, purification or separation of ammonia
    • C01C1/04—Preparation of ammonia by synthesis
    • C01C1/0405—Preparation of ammonia by synthesis from N2 and H2 in presence of a catalyst
    • C01C1/0417—Preparation of ammonia by synthesis from N2 and H2 in presence of a catalyst characterised by the synthesis reactor, e.g. arrangement of catalyst beds and heat exchangers in 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
    • B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
    • B01J8/0005—Catalytic processes under superatmospheric pressure
    • 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
    • B01J8/04—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 the fluid passing successively through two or more beds
    • B01J8/0446—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 the fluid passing successively through two or more beds the flow within the beds being predominantly vertical
    • 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
    • B01J8/04—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 the fluid passing successively through two or more beds
    • B01J8/0446—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 the fluid passing successively through two or more beds the flow within the beds being predominantly vertical
    • B01J8/0461—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 the fluid passing successively through two or more beds the flow within the beds being predominantly vertical in two or more cylindrical annular shaped beds
    • B01J8/0469—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 the fluid passing successively through two or more beds the flow within the beds being predominantly vertical in two or more cylindrical annular shaped beds the beds being superimposed one above the other
    • 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
    • B01J8/04—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 the fluid passing successively through two or more beds
    • B01J8/0496—Heating or cooling 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
    • B01J2208/00168—Controlling the temperature by indirect heat exchange with heat exchange elements outside the bed of solid particles
    • Y—GENERAL 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
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P20/00—Technologies relating to chemical industry
    • Y02P20/50—Improvements relating to the production of bulk chemicals
    • Y02P20/52—Improvements relating to the production of bulk chemicals using catalysts, e.g. selective catalysts

Landscapes

  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Organic Chemistry (AREA)
  • Analytical Chemistry (AREA)
  • Inorganic Chemistry (AREA)
  • Devices And Processes Conducted In The Presence Of Fluids And Solid Particles (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Physical Or Chemical Processes And Apparatus (AREA)
  • Exhaust Gas Treatment By Means Of Catalyst (AREA)
  • Chimneys And Flues (AREA)
  • Making Paper Articles (AREA)
  • Catalysts (AREA)
IL28758A 1966-10-18 1967-10-12 Reactor for the continuous performance of exothermic catalyzed reactions in the gas phase under high pressure IL28758A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
IT2896166 1966-10-18

Publications (1)

Publication Number Publication Date
IL28758A true IL28758A (en) 1971-11-29

Family

ID=11225109

Family Applications (1)

Application Number Title Priority Date Filing Date
IL28758A IL28758A (en) 1966-10-18 1967-10-12 Reactor for the continuous performance of exothermic catalyzed reactions in the gas phase under high pressure

Country Status (13)

Country Link
US (1) US3753662A (enExample)
JP (1) JPS5245671B1 (enExample)
BE (1) BE705266A (enExample)
CH (1) CH494589A (enExample)
CS (1) CS169751B2 (enExample)
DE (1) DE1667187C3 (enExample)
GB (1) GB1197516A (enExample)
GR (1) GR36634B (enExample)
IL (1) IL28758A (enExample)
NL (1) NL157513B (enExample)
NO (1) NO121334B (enExample)
SE (1) SE346069B (enExample)
YU (1) YU31932B (enExample)

Families Citing this family (18)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3918918A (en) * 1972-03-15 1975-11-11 Lummus Co Catalytic reactor
US4019871A (en) * 1974-09-30 1977-04-26 General Electric Company Recombiner apparatus
TR18747A (tr) * 1975-07-15 1977-08-02 Snam Progetti Yueksek termik duezeyli buhar ueretimiyle amonyagin sentezine mahsus radyal akisli reaktoer
IT1078798B (it) * 1976-09-24 1985-05-08 Tecnimont Spa Reattore per reazioni esotermiche catalizzate
JPS5841156U (ja) * 1981-09-14 1983-03-18 積水樹脂株式会社 農園芸支柱用線材支持キヤツプ
US4452760A (en) * 1982-01-18 1984-06-05 The M. W. Kellogg Company Horizontal ammonia converter
DE3302304A1 (de) * 1983-01-25 1984-07-26 Borsig Gmbh, 1000 Berlin Waermetauscher zum kuehlen von heissen gasen, insbesondere aus der ammoniak-synthese
CH665274A5 (de) * 1984-07-05 1988-04-29 Sulzer Ag Waermeuebertrager.
US4735780A (en) * 1986-07-15 1988-04-05 The M. W. Kellogg Company Ammonia synthesis converter
DE3725564A1 (de) * 1987-08-01 1989-02-09 Uhde Gmbh Verfahren und anlage zur durchfuehrung einer synthese, insbesondere zur synthese von ammoniak
FR2624115B1 (fr) * 1987-12-03 1990-04-13 Gaz De France Procede et appareil pour la conversion des hydrocarbures
DE3819451A1 (de) * 1988-06-08 1989-12-14 Uhde Gmbh Vorrichtung zur durchfuehrung exothermer, katalytischer gasreaktionen fuer die ammoniak- oder methanol-synthese
US5236671A (en) * 1990-09-24 1993-08-17 C. F. Braun, Inc. Apparatus for ammonia synthesis
DE102007024934B4 (de) 2007-05-29 2010-04-29 Man Dwe Gmbh Rohrbündelreaktoren mit Druckflüssigkeitskühlung
CN114423519B (zh) * 2019-10-25 2023-10-10 卡萨乐有限公司 用于氨的催化氧化的方法和反应器
LU103462B1 (de) 2024-11-25 2026-05-26 Thyssenkrupp Ag Kessel zur katalytischen Oxidation von Ammoniak sowie eine entsprechende Anlage und Verfahren
DE102024134717A1 (de) 2024-11-25 2026-05-28 Thyssenkrupp Ag Kessel zur katalytischen Oxidation von Ammoniak sowie eine entsprechende Anlage und Verfahren
WO2026109806A1 (de) 2024-11-25 2026-05-28 Thyssenkrupp Uhde Gmbh Kessel zur katalytischen oxidation von ammoniak sowie eine entsprechende anlage und verfahren

Family Cites Families (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2391315A (en) * 1945-12-18 Reactor
US2174318A (en) * 1936-04-14 1939-09-26 Henry Vogt Machine Co Unit tank heater
US2898183A (en) * 1954-03-18 1959-08-04 Montedison Spa Process and apparatus for performing exothermic reactions under high pressure and at elevated temperature

Also Published As

Publication number Publication date
JPS5245671B1 (enExample) 1977-11-17
SE346069B (enExample) 1972-06-26
US3753662A (en) 1973-08-21
DE1667187B2 (de) 1973-05-10
YU31932B (en) 1974-02-28
NL157513B (nl) 1978-08-15
NO121334B (enExample) 1971-02-15
DE1667187A1 (de) 1972-03-09
BE705266A (enExample) 1968-04-17
CH494589A (de) 1970-08-15
GR36634B (el) 1969-02-27
YU203867A (en) 1973-08-31
NL6713802A (enExample) 1968-04-19
DE1667187C3 (de) 1973-12-13
CS169751B2 (enExample) 1976-07-29
GB1197516A (en) 1970-07-08

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