PL113671B1 - Method of carrying out highly exothermic,catalytically accelerated chemical reactions - Google Patents

Method of carrying out highly exothermic,catalytically accelerated chemical reactions Download PDF

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Publication number
PL113671B1
PL113671B1 PL1978204474A PL20447478A PL113671B1 PL 113671 B1 PL113671 B1 PL 113671B1 PL 1978204474 A PL1978204474 A PL 1978204474A PL 20447478 A PL20447478 A PL 20447478A PL 113671 B1 PL113671 B1 PL 113671B1
Authority
PL
Poland
Prior art keywords
reactor
reaction
isothermal
adiabatic
adiabatic reactor
Prior art date
Application number
PL1978204474A
Other languages
English (en)
Polish (pl)
Other versions
PL204474A1 (pl
Original Assignee
Linde Ag
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 Linde Ag filed Critical Linde Ag
Publication of PL204474A1 publication Critical patent/PL204474A1/xx
Publication of PL113671B1 publication Critical patent/PL113671B1/pl

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Classifications

    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C29/00Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring
    • C07C29/15Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring by reduction of oxides of carbon exclusively
    • C07C29/151Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring by reduction of oxides of carbon exclusively with hydrogen or hydrogen-containing gases
    • C07C29/152Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring by reduction of oxides of carbon exclusively with hydrogen or hydrogen-containing gases characterised by the reactor used
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J8/00Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
    • B01J8/02Chemical 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
    • B01J8/0285Heating or cooling the reactor
    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01CAMMONIA; CYANOGEN; COMPOUNDS THEREOF
    • C01C1/00Ammonia; Compounds thereof
    • C01C1/02Preparation, purification or separation of ammonia
    • C01C1/04Preparation of ammonia by synthesis in the gas phase
    • C01C1/0405Preparation of ammonia by synthesis in the gas phase from N2 and H2 in presence of a catalyst
    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01CAMMONIA; CYANOGEN; COMPOUNDS THEREOF
    • C01C1/00Ammonia; Compounds thereof
    • C01C1/02Preparation, purification or separation of ammonia
    • C01C1/04Preparation of ammonia by synthesis in the gas phase
    • C01C1/0405Preparation of ammonia by synthesis in the gas phase from N2 and H2 in presence of a catalyst
    • C01C1/0482Process control; Start-up or cooling-down procedures
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C1/00Preparation of hydrocarbons from one or more compounds, none of them being a hydrocarbon
    • C07C1/02Preparation of hydrocarbons from one or more compounds, none of them being a hydrocarbon from oxides of a carbon
    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P20/00Technologies relating to chemical industry
    • Y02P20/50Improvements relating to the production of bulk chemicals
    • Y02P20/52Improvements relating to the production of bulk chemicals using catalysts, e.g. selective catalysts

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Engineering & Computer Science (AREA)
  • Analytical Chemistry (AREA)
  • Inorganic Chemistry (AREA)
  • General Chemical & Material Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Automation & Control Theory (AREA)
  • Physical Or Chemical Processes And Apparatus (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
PL1978204474A 1977-02-08 1978-02-06 Method of carrying out highly exothermic,catalytically accelerated chemical reactions PL113671B1 (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
DE2705141A DE2705141C2 (de) 1977-02-08 1977-02-08 Verfahren zur Herstellung von Methan oder Methanol

Publications (2)

Publication Number Publication Date
PL204474A1 PL204474A1 (pl) 1978-10-09
PL113671B1 true PL113671B1 (en) 1980-12-31

Family

ID=6000593

Family Applications (1)

Application Number Title Priority Date Filing Date
PL1978204474A PL113671B1 (en) 1977-02-08 1978-02-06 Method of carrying out highly exothermic,catalytically accelerated chemical reactions

Country Status (3)

Country Link
DE (1) DE2705141C2 (de)
PL (1) PL113671B1 (de)
ZA (1) ZA78756B (de)

Families Citing this family (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE3121991C2 (de) * 1981-06-03 1985-11-28 Kernforschungsanlage Jülich GmbH, 5170 Jülich Verfahren zur Erzeugung von überhitztem Dampf im Wärmeaustausch mit einem katalytisch zu methanisierenden, Kohlenmonoxid, Kohlendioxid und Wasserstoff enthaltenden Synthesegas sowie Vorrichtung zur Durchführung des Verfahrens
DE3612734C1 (de) * 1986-04-16 1987-12-17 Kernforschungsanlage Juelich Verfahren zur katalytischen Methanisierung eines Kohlenmonoxid,Kohlendioxid und Wasserstoff enthaltenden Synthesegases und Reaktor zur Methanisierung
DE3725564A1 (de) * 1987-08-01 1989-02-09 Uhde Gmbh Verfahren und anlage zur durchfuehrung einer synthese, insbesondere zur synthese von ammoniak
EP0807602A1 (de) * 1996-05-13 1997-11-19 Haldor Topsoe A/S Verfahren zur Herstellung von Ammonia
GB0113078D0 (en) 2001-05-30 2001-07-18 Kvaerner Process Tech Ltd Process and plant
DE102018113737A1 (de) 2018-06-08 2019-12-12 Man Energy Solutions Se Verfahren und Reaktorsystem zur Durchführung katalytischer Gasphasenreaktionen
DE102018113735A1 (de) 2018-06-08 2019-12-12 Man Energy Solutions Se Verfahren, Rohrbündelreaktor und Reaktorsystem zur Durchführung katalytischer Gasphasenreaktionen

Family Cites Families (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2795558A (en) * 1953-01-15 1957-06-11 Texas Co Production of ammonia synthesis feed gas
GB904940A (en) * 1960-08-30 1962-09-05 Hans Joachim Zimmer Process for the thermal-catalytic conversion of gaseous or liquid hydrocarbons into gases consisting mainly of carbon monoxide, hydrogen and possibly methane
NL297554A (de) * 1962-09-07
GB1053788A (de) * 1964-05-27 1900-01-01
US3843512A (en) * 1967-09-01 1974-10-22 Chevron Res Hydrogen manufacture using centrifugal compressors
DE2043417A1 (de) * 1969-09-05 1971-04-29 Alco Standard Corp , Cleveland, Ohio (V St A ) Verfahren und Vorrichtung zum Her stellen von Wasserstoff und Wasserstoff enthaltende Gasgemische

Also Published As

Publication number Publication date
PL204474A1 (pl) 1978-10-09
ZA78756B (en) 1979-01-31
DE2705141A1 (de) 1978-08-10
DE2705141C2 (de) 1984-09-13

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