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GB474191A - Improvements in the cooling of gases - Google Patents

Improvements in the cooling of gases

Info

Publication number
GB474191A
GB474191A GB1938/37A GB193837A GB474191A GB 474191 A GB474191 A GB 474191A GB 1938/37 A GB1938/37 A GB 1938/37A GB 193837 A GB193837 A GB 193837A GB 474191 A GB474191 A GB 474191A
Authority
GB
United Kingdom
Prior art keywords
gases
water
sulphur
temperature
liquid
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
GB1938/37A
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.)
IG Farbenindustrie AG
Original Assignee
IG Farbenindustrie 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 IG Farbenindustrie AG filed Critical IG Farbenindustrie AG
Publication of GB474191A publication Critical patent/GB474191A/en
Expired legal-status Critical Current

Links

Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28CHEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA COME INTO DIRECT CONTACT WITHOUT CHEMICAL INTERACTION
    • F28C3/00Other direct-contact heat-exchange apparatus
    • F28C3/06Other direct-contact heat-exchange apparatus the heat-exchange media being a liquid and a gas or vapour

Landscapes

  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Treating Waste Gases (AREA)

Abstract

Hot gases or vapours are cooled by injecting a liquid of a different chemical nature, preferably water, in a finely distributed state at a temperature which is (a) equal to or above its boiling point at the pressure of the gases to be cooled, and (b) below the temperature of the said gases. The complete evaporation of the injected water thus ensured is useful in processes, such as the obtaining of gases by roasting pyrites, where the presence of liquid water is deleterious to the constructional materials of the apparatus. The water, heated directly or indirectly, may be forced through atomizing nozzles arranged in known manner. The superheated pressure water may be obtained from the feed water for a boiler. Preferably the temperature of the liquid under pressure should be at least 5 DEG C. above its boiling point at the gas pressure. The invention is applicable to exothermic catalytic reactions in which the main part of the gases involved is converted by means of a first contact layer, the final conversion being effected by means of a second contact layer and the gases being cooled between the two stages. Such processes are used, for example, for producing hydrogen and carbon monoxide from hydrocarbons and steam, or for oxidizing sulphur dioxide, in the synthesis of ammonia from nitrogen and hydrogen, liquefied ammonia being preferably injected in this case between the contact layers for cooling the gas, or in the synthesis of hydrocarbons from carbon monoxide and hydrogen, superheated hydrocarbons being preferably injected between two or more contact layers. The invention is also useful when products formed are to be prevented from decomposing by cooling them rapidly, as in the production of oxides of nitrogen by combustion of ammonia in the production of unsaturated hydrocarbons by thermal decomposition. A quantitative example is given to illustrate the application to the cooling of sulphur-containing gases obtained by the Claus process. These gases having a temperature of 400 DEG C. are cooled down to 150 DEG C. by the injection of finely atomized water at a temperature of 125 DEG C., the whole of the sulphur being condensed into the liquid phase. One third of the sulphur precipitates as a liquid in the vaporizer sump and is continuously withdrawn by means of a heated overflow pipe; the bulk of the sulphur is separated on an electrofilter arranged behind the cooler.
GB1938/37A 1936-01-24 1937-01-22 Improvements in the cooling of gases Expired GB474191A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
DE474191X 1936-01-24

Publications (1)

Publication Number Publication Date
GB474191A true GB474191A (en) 1937-10-27

Family

ID=6541678

Family Applications (1)

Application Number Title Priority Date Filing Date
GB1938/37A Expired GB474191A (en) 1936-01-24 1937-01-22 Improvements in the cooling of gases

Country Status (1)

Country Link
GB (1) GB474191A (en)

Cited By (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2419309A (en) * 1944-01-13 1947-04-22 Stauffer Chemical Co Sulphur production
US2419310A (en) * 1944-11-07 1947-04-22 Stauffer Chemical Co Sulphur production
US2432099A (en) * 1943-07-24 1947-12-09 Standard Oil Dev Co Method of preparing aromatic amines
US2448279A (en) * 1944-08-23 1948-08-31 Kellogg M W Co Synthesis of organic compounds
US2475214A (en) * 1944-10-12 1949-07-05 Standard Oil Dev Co Hydrocarbon synthesis
US2490463A (en) * 1945-10-22 1949-12-06 Phillips Petroleum Co Synthesis of hydrocarbons
US2521538A (en) * 1945-06-20 1950-09-05 Texaco Development Corp Process for synthesis of hydrocarbons and the like
US2526934A (en) * 1947-01-20 1950-10-24 Phillips Petroleum Co Removal of exothermic heat of reaction
US2594149A (en) * 1948-03-05 1952-04-22 Great Lakes Carbon Corp Sulfur recovery
US2620356A (en) * 1943-07-17 1952-12-02 Standard Oil Dev Co Production of aromatic amines
US2767061A (en) * 1953-06-02 1956-10-16 Allied Chem & Dye Corp Continuous process for cooling liquid sulfur
CH710092A1 (en) * 2014-09-10 2016-03-15 Robert Stucki A method for rapid cooling of exhaust gases and injection cooler.

Cited By (13)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2620356A (en) * 1943-07-17 1952-12-02 Standard Oil Dev Co Production of aromatic amines
US2432099A (en) * 1943-07-24 1947-12-09 Standard Oil Dev Co Method of preparing aromatic amines
US2419309A (en) * 1944-01-13 1947-04-22 Stauffer Chemical Co Sulphur production
US2448279A (en) * 1944-08-23 1948-08-31 Kellogg M W Co Synthesis of organic compounds
US2475214A (en) * 1944-10-12 1949-07-05 Standard Oil Dev Co Hydrocarbon synthesis
US2419310A (en) * 1944-11-07 1947-04-22 Stauffer Chemical Co Sulphur production
US2521538A (en) * 1945-06-20 1950-09-05 Texaco Development Corp Process for synthesis of hydrocarbons and the like
US2490463A (en) * 1945-10-22 1949-12-06 Phillips Petroleum Co Synthesis of hydrocarbons
US2526934A (en) * 1947-01-20 1950-10-24 Phillips Petroleum Co Removal of exothermic heat of reaction
US2594149A (en) * 1948-03-05 1952-04-22 Great Lakes Carbon Corp Sulfur recovery
US2767061A (en) * 1953-06-02 1956-10-16 Allied Chem & Dye Corp Continuous process for cooling liquid sulfur
CH710092A1 (en) * 2014-09-10 2016-03-15 Robert Stucki A method for rapid cooling of exhaust gases and injection cooler.
EP2995363A1 (en) 2014-09-10 2016-03-16 Robert Stucki Method for scrubbing gases, rapid cooling of gases, and for heat extraction

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