GB688096A - Improvements in or relating to method of and apparatus for gasifying carbonaceous solids - Google Patents

Improvements in or relating to method of and apparatus for gasifying carbonaceous solids

Info

Publication number
GB688096A
GB688096A GB13052/51A GB1305251A GB688096A GB 688096 A GB688096 A GB 688096A GB 13052/51 A GB13052/51 A GB 13052/51A GB 1305251 A GB1305251 A GB 1305251A GB 688096 A GB688096 A GB 688096A
Authority
GB
United Kingdom
Prior art keywords
fed
solids
vessel
withdrawn
fluidized
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
GB13052/51A
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.)
Consolidation Coal Co
Pittsburgh Consolidation Coal Co
Original Assignee
Consolidation Coal Co
Pittsburgh Consolidation Coal Co
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 Consolidation Coal Co, Pittsburgh Consolidation Coal Co filed Critical Consolidation Coal Co
Publication of GB688096A publication Critical patent/GB688096A/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
    • C10J3/00Production of combustible gases containing carbon monoxide from solid carbonaceous fuels
    • C10J3/02Fixed-bed gasification of lump fuel
    • C10J3/20Apparatus; Plants
    • 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
    • C10J3/00Production of combustible gases containing carbon monoxide from solid carbonaceous fuels
    • C10J3/46Gasification of granular or pulverulent flues in suspension
    • C10J3/48Apparatus; Plants
    • C10J3/482Gasifiers with stationary fluidised bed
    • 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
    • C10J2300/00Details of gasification processes
    • C10J2300/09Details of the feed, e.g. feeding of spent catalyst, inert gas or halogens
    • C10J2300/0913Carbonaceous raw material
    • C10J2300/093Coal
    • C10J2300/0933Coal fines for producing water gas

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Combustion & Propulsion (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Organic Chemistry (AREA)
  • Devices And Processes Conducted In The Presence Of Fluids And Solid Particles (AREA)

Abstract

688,096. Gasifying solid carbonaceous materials. PITTSBURGH CONSOLIDATION COAL CO. June 1, 1951 [June 23, 1950], No. 13052/51. Class 55 (i). In a fluidized process for gasifying solid carbonaceous materials such as coke, coal, oil shale and lignite by means of steam and a gas containing oxygen, particulate carbonaceous solids are fed upwardly by a worm gear type stoker 17 through an annular zone 19 between an outer vessel 10 and an inner vessel 20 to overflow into a fluidized gasification zone in the vessel 20, the gaseous products being withdrawn downwardly through the annular zone 19 to an outlet pipe 30 thereby to preheat the solids fed to the gasification and to remove entrained fine solids. Steam and oxygen are fed through the line 26 to the gasification zone which is maintained at a temperature of 1800-2000‹F and a pressure of 20 atmospheres ; ash is withdrawn through a line 32. In a modification the preheating and fluidized zones may be in separate vessels in side by side relationship, the carbonaceous solids being fed upwardly through one vessel and overflowing into the other and the withdrawn gases passing downwardly through the upwardly fed carbonaceous solids.
GB13052/51A 1950-06-23 1951-06-01 Improvements in or relating to method of and apparatus for gasifying carbonaceous solids Expired GB688096A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US688096XA 1950-06-23 1950-06-23

Publications (1)

Publication Number Publication Date
GB688096A true GB688096A (en) 1953-02-25

Family

ID=22084828

Family Applications (1)

Application Number Title Priority Date Filing Date
GB13052/51A Expired GB688096A (en) 1950-06-23 1951-06-01 Improvements in or relating to method of and apparatus for gasifying carbonaceous solids

Country Status (1)

Country Link
GB (1) GB688096A (en)

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