GB279059A - Improvements in or relating to the manufacture of mixed water gas and distillation gas from fuels of volatile content - Google Patents

Improvements in or relating to the manufacture of mixed water gas and distillation gas from fuels of volatile content

Info

Publication number
GB279059A
GB279059A GB25513/27A GB2551327A GB279059A GB 279059 A GB279059 A GB 279059A GB 25513/27 A GB25513/27 A GB 25513/27A GB 2551327 A GB2551327 A GB 2551327A GB 279059 A GB279059 A GB 279059A
Authority
GB
United Kingdom
Prior art keywords
gas
generator
run
water gas
storage
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
GB25513/27A
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.)
Humphreys and Glasgow Ltd
Original Assignee
Humphreys and Glasgow Ltd
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 Humphreys and Glasgow Ltd filed Critical Humphreys and Glasgow Ltd
Publication of GB279059A publication Critical patent/GB279059A/en
Expired legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10JPRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
    • C10J1/00Production of fuel gases by carburetting air or other gases without pyrolysis
    • C10J1/213Carburetting by pyrolysis of solid carbonaceous material in a carburettor

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Combustion & Propulsion (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Organic Chemistry (AREA)
  • Processing Of Solid Wastes (AREA)

Abstract

279,059. Humphreys & Glasgow, Ltd., (Assignees of Chrisman, C. S.). Oct. 13, 1926, [Convention date]. Producers.-Combustible gas comprising a mixture of distillation gas and carburetted water gas is obtained by blasting the lower part of a fuel bed, making an up-run through the fuel bed. carburetting and fixing other gas by heat stored during the blasting and passing the carburetted gas and the water gas from the up-run through the upper part of the fuel bed to generate coal gas which is mixed with the other combustible gases. Two generators 1, 2 are blasted in parallel, the blast gases traversing the gasification zones 11 only, and passing through superheaters 3, 4 and regenerators and carburettors 5, 6, to which air is supplied to support combustion, before leaving by stack valves 29. A down-run is then made on one generator, say 1, and an uprun on generator 2, and, by suitable adjustment of the valves, the water gas from the generator 1 passes through conduit 17 to the regenerator chamber 25 and carburetting chamber 24 of the carburettor 6 from which the gas and oil vapours pass to and are fixed in superheater 4 before entering by conduit 14 the generator 2 where they mix with the up-run water gas and distil the fuel in the upper part of the generator; the mixed gases pass through conduit 20 to condensing apparatus and storage. 'The steam runs are now reversed and an up-run made in generator 1 while a down-run is made in generator 2, the gases taking a path similar to that described but through the alternative fixers and carburettors. In a modified process, after the parallel blast and during a down-run on generator 1, steam is admitted by pipe 32 to vessel 5 and passes through heater 3 to generator 1 and is used in the gas making, in this case it is necessary to make the next step a parallel blasting before the alternative operation is commenced. Supplementary gas from storage may be admitted through pipe 31<b>. In the apparatus shown in Fig. 4, the generator 2<a> is blasted upwards and and gas passes directly into superheater 4<a> and is burned therein, the hot gases passing through the carburettor 5a to the stack 18<a>. During the run, steam is admitted to the base of the generator, the water gas going through the carbonization zone 3a, gas being simultaneously drawn from storage through pipe 20<a>, carburetted in chamber 5a, fixed in superheater 4a and passed together with the water gas through the carbonization zone to the wash box 8<a> and storage. A down-run is then made, the water gas passing by conduit 13<a> to the wash box and storage. Steam or water may be admitted by pipe 28<a>.
GB25513/27A 1926-10-13 1927-09-27 Improvements in or relating to the manufacture of mixed water gas and distillation gas from fuels of volatile content Expired GB279059A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US279059XA 1926-10-13 1926-10-13

Publications (1)

Publication Number Publication Date
GB279059A true GB279059A (en) 1928-05-17

Family

ID=21840449

Family Applications (1)

Application Number Title Priority Date Filing Date
GB25513/27A Expired GB279059A (en) 1926-10-13 1927-09-27 Improvements in or relating to the manufacture of mixed water gas and distillation gas from fuels of volatile content

Country Status (1)

Country Link
GB (1) GB279059A (en)

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