GB800812A - Method and apparatus for the discharge of molten material from gas producers or the like - Google Patents

Method and apparatus for the discharge of molten material from gas producers or the like

Info

Publication number
GB800812A
GB800812A GB10980/55A GB1098055A GB800812A GB 800812 A GB800812 A GB 800812A GB 10980/55 A GB10980/55 A GB 10980/55A GB 1098055 A GB1098055 A GB 1098055A GB 800812 A GB800812 A GB 800812A
Authority
GB
United Kingdom
Prior art keywords
producer
slag
chamber
gas
steam
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
GB10980/55A
Inventor
Julius Schierenbeck
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.)
Kohlenscheidungs GmbH
Original Assignee
Kohlenscheidungs GmbH
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 Kohlenscheidungs GmbH filed Critical Kohlenscheidungs GmbH
Priority to GB10980/55A priority Critical patent/GB800812A/en
Publication of GB800812A publication Critical patent/GB800812A/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
    • C10J3/06Continuous processes
    • C10J3/08Continuous processes with ash-removal in liquid state
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P20/00Technologies relating to chemical industry
    • Y02P20/10Process efficiency
    • Y02P20/129Energy recovery, e.g. by cogeneration, H2recovery or pressure recovery turbines

Abstract

800,812. Gas producers ; discharging molten residues. HOHLENSCHEIDUNGS-G.m.b.H. April 15, 1955, No. 10980/55. Classes 51 (1) and 51 (2). A method of controlling the continuous discharge of molten material from gas producers &c. utilizes means which creates a pressure, acting at the slag discharge opening mouth, which exceeds, and operates against, the gas pressure in the producer. In the producer shown, slag is discharged through an outlet 2, Fig. 1, into a water bath 26, and the resulting granulated material is moved to a conveyer 11, Fig. 2, by a conveyer 8 operating in a waterfilled trough 7. The bath 26 is in a pressure chamber 5 in which the pressure is kept, during producer operation, at a value higher than that of the gas in the producer. Variation in the slag level 3 or 3<SP>1</SP> is effected by varying the water head h1 in the slag disposal system. The space above the water in the chamber 5 is filled with steam, evolved, after an initial introduction of steam, through a valve-controlled opening 14 on starting up the producer, as the molten slag drops into the bath. Steam surplus to chamber pressurizing requirements is passed through a pipe 16 and spiral tube arrangements 22, 22<SP>1</SP>, 22<SP>11</SP>, to cool the hot gases leaving the producer through a duct 23. The steam, which passes from the arrangement 22<SP>11</SP> to the producer via a nozzle 25, is also used to heat the producer air supply in a duct 27<SP>1</SP>. Make-up water is fed to the chamber 5 and the slag disposal system through a valve-controlled main 17. In another producer, the slag passes from the chamber 5, Fig. 3, to a chamber 29, Fig. 5, at the top of which is an outlet for slag discharge on to the conveyer 11. The level of the outlet, which may be varied, determines the surface level of the slag in the producer. Prior to furnace operation, the chambers are heated by a gas flame introduced and withdrawn through pipes 32, 33, respectively, whilst on cessation of operation the plug is drained-off through hole 34. In applying the invention to a producer in which iron smelting is effected, the iron and slag may be discharged by means of the devices of Figs. 3, 5, and 1, 2, respectively.
GB10980/55A 1955-04-15 1955-04-15 Method and apparatus for the discharge of molten material from gas producers or the like Expired GB800812A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
GB10980/55A GB800812A (en) 1955-04-15 1955-04-15 Method and apparatus for the discharge of molten material from gas producers or the like

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
GB10980/55A GB800812A (en) 1955-04-15 1955-04-15 Method and apparatus for the discharge of molten material from gas producers or the like

Publications (1)

Publication Number Publication Date
GB800812A true GB800812A (en) 1958-09-03

Family

ID=9977844

Family Applications (1)

Application Number Title Priority Date Filing Date
GB10980/55A Expired GB800812A (en) 1955-04-15 1955-04-15 Method and apparatus for the discharge of molten material from gas producers or the like

Country Status (1)

Country Link
GB (1) GB800812A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0129256A2 (en) * 1983-06-20 1984-12-27 Hylsa, S.A. Process for production of gaseous mixture of carbon monoxide and hydrogen and melter-gasifier system for carrying out the process
WO2002057396A1 (en) * 2000-12-21 2002-07-25 Nesi Plant S.A. Process and apparatus for the production of hydrogen and carbon dioxide from the gasification of raw materials

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0129256A2 (en) * 1983-06-20 1984-12-27 Hylsa, S.A. Process for production of gaseous mixture of carbon monoxide and hydrogen and melter-gasifier system for carrying out the process
EP0129256A3 (en) * 1983-06-20 1985-10-30 Hylsa, S.A. Process for production of gaseous mixture of carbon monoxide and hydrogen and melter-gasifier system for carrying out the process
WO2002057396A1 (en) * 2000-12-21 2002-07-25 Nesi Plant S.A. Process and apparatus for the production of hydrogen and carbon dioxide from the gasification of raw materials

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