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GB673164A - Improvements in the production of gases containing carbon monoxide and hydrogen from finely divided solid fuels - Google Patents

Improvements in the production of gases containing carbon monoxide and hydrogen from finely divided solid fuels

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Publication number
GB673164A
GB673164AGB31419/49AGB3141949AGB673164AGB 673164 AGB673164 AGB 673164AGB 31419/49 AGB31419/49 AGB 31419/49AGB 3141949 AGB3141949 AGB 3141949AGB 673164 AGB673164 AGB 673164A
Authority
GB
United Kingdom
Prior art keywords
fuel
jet
oxygen
chamber
per cent
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
GB31419/49A
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.)
Beazer East Inc
Original Assignee
Koppers Co Inc
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 Koppers Co IncfiledCriticalKoppers Co Inc
Publication of GB673164ApublicationCriticalpatent/GB673164A/en
Expiredlegal-statusCriticalCurrent

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Abstract

673,164. Gasifying powdered fuel. KOPPERS CO., Inc. Dec. 7, 1949 [Dec. 7,1948], No. 31419/49. Classes 55 (i) and 55 (ii). Combustible gas is produced by forming a suspension in oxygen or oxygen enriched air under pressure, of a finely divided fuel such as coal or lignite, injecting the suspension as a jet into an internally heated chamber where the fuel partly burns, introducing steam or carbon dioxide under the same pressure around the jet, so that it reacts with the gases and unburnt fuel therefrom to form a combustible gas. The process is similar to that described in' Specification 673,161 except that the earlier process is conducted at atmospheric pressure. In the apparatus shown, powdered fuel from hoppers 2 and 3 and oxygen under pressure from pipe 8 are mixed in mixer 7 and injected through a pipe 10 to form a jet in a conical gasification chamber 13 which is internally heated so. that the fuel ignites and is partly burnt in the jet. An annular orifice 14 surrounds the pipe 10 and admits steam, at the same pressure as the oxygen and preheated to 450-500‹ C. by combustion gases from burners 23, as an envelope around the jet, thus protecting the walls of the chamber from the high temperature thereof. The gases and unburnt fuel from the fuel-oxygen jet react with the steam lower in the chamber to form a gas of composition CO 2 11.8 per cent; CO 43.1 per cent; H 2 43.1 per cent; N 2 &c. 2.0 per cent. To prevent methane formation, the gas is cooled to 500‹ C. by cold gas entering at 28 and then passed in series through water jacketed chambers 22 and 18 where the solid residues are deposited and finally through a fire-tube boiler 19 to outlet 21 which is controlled by a valve so as to maintain a steady pressure of between 5 and 20 atmospheres in chamber 13.
GB31419/49A1948-12-071949-12-07Improvements in the production of gases containing carbon monoxide and hydrogen from finely divided solid fuelsExpiredGB673164A (en)

Applications Claiming Priority (1)

Application NumberPriority DateFiling DateTitle
CH673164X1948-12-07

Publications (1)

Publication NumberPublication Date
GB673164Atrue GB673164A (en)1952-06-04

Family

ID=4527856

Family Applications (1)

Application NumberTitlePriority DateFiling Date
GB31419/49AExpiredGB673164A (en)1948-12-071949-12-07Improvements in the production of gases containing carbon monoxide and hydrogen from finely divided solid fuels

Country Status (1)

CountryLink
GB (1)GB673164A (en)

Cited By (10)

* Cited by examiner, † Cited by third party
Publication numberPriority datePublication dateAssigneeTitle
US4247302A (en)*1979-07-131981-01-27Texaco Inc.Process for gasification and production of by-product superheated steam
US4248604A (en)*1979-07-131981-02-03Texaco Inc.Gasification process
US4251228A (en)*1979-05-301981-02-17Texaco Development CorporationProduction of cleaned and cooled synthesis gas
US4289502A (en)*1979-05-301981-09-15Texaco Development CorporationApparatus for the production of cleaned and cooled synthesis gas
US4309196A (en)1979-12-191982-01-05M.A.N. Maschinenfabrik Augsburg-Nurnberg AktiengesellschaftCoal gasification apparatus
US4326856A (en)*1979-05-301982-04-27Texaco Development CorporationProduction of cleaned and cooled synthesis gas
US4328008A (en)*1979-05-301982-05-04Texaco Development CorporationMethod for the production of cleaned and cooled synthesis gas
US4328006A (en)*1979-05-301982-05-04Texaco Development CorporationApparatus for the production of cleaned and cooled synthesis gas
US4377394A (en)*1979-05-301983-03-22Texaco Development CorporationApparatus for the production of cleaned and cooled synthesis gas
EP0258943B1 (en)*1986-08-291992-04-08Shell Internationale Researchmaatschappij B.V.Process and apparatus for the preparation of synthesis gas

Cited By (10)

* Cited by examiner, † Cited by third party
Publication numberPriority datePublication dateAssigneeTitle
US4251228A (en)*1979-05-301981-02-17Texaco Development CorporationProduction of cleaned and cooled synthesis gas
US4289502A (en)*1979-05-301981-09-15Texaco Development CorporationApparatus for the production of cleaned and cooled synthesis gas
US4326856A (en)*1979-05-301982-04-27Texaco Development CorporationProduction of cleaned and cooled synthesis gas
US4328008A (en)*1979-05-301982-05-04Texaco Development CorporationMethod for the production of cleaned and cooled synthesis gas
US4328006A (en)*1979-05-301982-05-04Texaco Development CorporationApparatus for the production of cleaned and cooled synthesis gas
US4377394A (en)*1979-05-301983-03-22Texaco Development CorporationApparatus for the production of cleaned and cooled synthesis gas
US4247302A (en)*1979-07-131981-01-27Texaco Inc.Process for gasification and production of by-product superheated steam
US4248604A (en)*1979-07-131981-02-03Texaco Inc.Gasification process
US4309196A (en)1979-12-191982-01-05M.A.N. Maschinenfabrik Augsburg-Nurnberg AktiengesellschaftCoal gasification apparatus
EP0258943B1 (en)*1986-08-291992-04-08Shell Internationale Researchmaatschappij B.V.Process and apparatus for the preparation of synthesis gas

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