GB739483A - Method of carrying out exothermic chemical reactions in the gaseous phase - Google Patents

Method of carrying out exothermic chemical reactions in the gaseous phase

Info

Publication number
GB739483A
GB739483A GB6984/52A GB698452A GB739483A GB 739483 A GB739483 A GB 739483A GB 6984/52 A GB6984/52 A GB 6984/52A GB 698452 A GB698452 A GB 698452A GB 739483 A GB739483 A GB 739483A
Authority
GB
United Kingdom
Prior art keywords
turbine
chemical reactions
reaction
acetaldehyde
methanol
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
GB6984/52A
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.)
Individual
Original Assignee
Individual
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 Individual filed Critical Individual
Publication of GB739483A publication Critical patent/GB739483A/en
Expired legal-status Critical Current

Links

Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F02COMBUSTION ENGINES; HOT-GAS OR COMBUSTION-PRODUCT ENGINE PLANTS
    • F02CGAS-TURBINE PLANTS; AIR INTAKES FOR JET-PROPULSION PLANTS; CONTROLLING FUEL SUPPLY IN AIR-BREATHING JET-PROPULSION PLANTS
    • F02C6/00Plural gas-turbine plants; Combinations of gas-turbine plants with other apparatus; Adaptations of gas-turbine plants for special use
    • F02C6/04Gas-turbine plants providing heated or pressurised working fluid for other apparatus, e.g. without mechanical power output
    • F02C6/10Gas-turbine plants providing heated or pressurised working fluid for other apparatus, e.g. without mechanical power output supplying working fluid to a user, e.g. a chemical process, which returns working fluid to a turbine of the plant
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J3/00Processes of utilising sub-atmospheric or super-atmospheric pressure to effect chemical or physical change of matter; Apparatus therefor
    • B01J3/06Processes using ultra-high pressure, e.g. for the formation of diamonds; Apparatus therefor, e.g. moulds or dies
    • B01J3/08Application of shock waves for chemical reactions or for modifying the crystal structure of substances

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Crystallography & Structural Chemistry (AREA)
  • Organic Chemistry (AREA)
  • General Chemical & Material Sciences (AREA)
  • Combustion & Propulsion (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)

Abstract

<PICT:0739483/III/1> Exothermic gas-phase catalytic chemical reactions are carried out in the expansion space of a turbine device, in order to transform the chemical energy liberated into kinetic energy. The reaction may take place between the rotor and stator blades of the turbine, and the catalyst may be suspended in the reaction space or fixed to the walls thereof. An inert gas may be added to the reactants. As shown, sulphur dioxide and oxygen are compressed in compressors 1, 2 respectively and reacted at 500 DEG C. in turbine reactor 3 to form sulphur trioxide; the rotor and the stator of the turbine are coated with platinum. The reaction product under a lower pressure is passed through sulphuric acid in absorber 5 to remove sulphur trioxide and then supplied to gas turbine 6. Reference is also made to the oxidation of ammonia to nitrogen oxides, the Fischer-Tropsch process, the synthesis of methanol, and the oxidation of methanol to formaldehyde, ethyl alcohol to acetaldehyde, and acetaldehyde to acetic acid.
GB6984/52A 1951-03-20 1952-03-18 Method of carrying out exothermic chemical reactions in the gaseous phase Expired GB739483A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
SE739483X 1951-03-20

Publications (1)

Publication Number Publication Date
GB739483A true GB739483A (en) 1955-11-02

Family

ID=20319793

Family Applications (1)

Application Number Title Priority Date Filing Date
GB6984/52A Expired GB739483A (en) 1951-03-20 1952-03-18 Method of carrying out exothermic chemical reactions in the gaseous phase

Country Status (1)

Country Link
GB (1) GB739483A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6180078B1 (en) * 1997-12-09 2001-01-30 Outokumpu Oyj Method for thermally regenerating spent acid
CN106762142A (en) * 2016-11-29 2017-05-31 沈阳黎明航空发动机(集团)有限责任公司 A kind of utilization gas turbine manufactures the device of diamond

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6180078B1 (en) * 1997-12-09 2001-01-30 Outokumpu Oyj Method for thermally regenerating spent acid
ES2154998A1 (en) * 1997-12-09 2001-04-16 Outokumpu Oy Method for thermally regenerating spent acid
CN106762142A (en) * 2016-11-29 2017-05-31 沈阳黎明航空发动机(集团)有限责任公司 A kind of utilization gas turbine manufactures the device of diamond

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