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EP0129256A2 - Verfahren zur Herstellung einer Mischung von Kohlenstoffmonoxyd und Wasserstoff und Schmelzbadvergaser - Google Patents

Verfahren zur Herstellung einer Mischung von Kohlenstoffmonoxyd und Wasserstoff und Schmelzbadvergaser Download PDF

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Publication number
EP0129256A2
EP0129256A2 EP84107105A EP84107105A EP0129256A2 EP 0129256 A2 EP0129256 A2 EP 0129256A2 EP 84107105 A EP84107105 A EP 84107105A EP 84107105 A EP84107105 A EP 84107105A EP 0129256 A2 EP0129256 A2 EP 0129256A2
Authority
EP
European Patent Office
Prior art keywords
slag
melter
gasifier
molten
water
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.)
Withdrawn
Application number
EP84107105A
Other languages
English (en)
French (fr)
Other versions
EP0129256A3 (de
Inventor
Ricardo Viramontes-Brown
Jorge Domingo Berrun-Castanon
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.)
Hylsa SA de CV
Original Assignee
Hylsa SA de CV
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 Hylsa SA de CV filed Critical Hylsa SA de CV
Publication of EP0129256A2 publication Critical patent/EP0129256A2/de
Publication of EP0129256A3 publication Critical patent/EP0129256A3/de
Withdrawn legal-status Critical Current

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Classifications

    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10J—PRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
    • C10J3/00—Production of combustible gases containing carbon monoxide from solid carbonaceous fuels
    • C10J3/57—Gasification using molten salts or metals
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10K—PURIFYING OR MODIFYING THE CHEMICAL COMPOSITION OF COMBUSTIBLE GASES CONTAINING CARBON MONOXIDE
    • C10K1/00—Purifying combustible gases containing carbon monoxide
    • C10K1/04—Purifying combustible gases containing carbon monoxide by cooling to condense non-gaseous materials
    • C10K1/06—Purifying combustible gases containing carbon monoxide by cooling to condense non-gaseous materials combined with spraying with water
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10K—PURIFYING OR MODIFYING THE CHEMICAL COMPOSITION OF COMBUSTIBLE GASES CONTAINING CARBON MONOXIDE
    • C10K1/00—Purifying combustible gases containing carbon monoxide
    • C10K1/08—Purifying combustible gases containing carbon monoxide by washing with liquids; Reviving the used wash liquors
    • C10K1/10—Purifying combustible gases containing carbon monoxide by washing with liquids; Reviving the used wash liquors with aqueous liquids
    • C10K1/101—Purifying combustible gases containing carbon monoxide by washing with liquids; Reviving the used wash liquors with aqueous liquids with water only
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10J—PRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
    • C10J2200/00—Details of gasification apparatus
    • C10J2200/15—Details of feeding means
    • C10J2200/152—Nozzles or lances for introducing gas, liquids or suspensions
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10J—PRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
    • C10J2300/00—Details of gasification processes
    • C10J2300/09—Details of the feed, e.g. feeding of spent catalyst, inert gas or halogens
    • C10J2300/0913—Carbonaceous raw material
    • C10J2300/093—Coal
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10J—PRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
    • C10J2300/00—Details of gasification processes
    • C10J2300/09—Details of the feed, e.g. feeding of spent catalyst, inert gas or halogens
    • C10J2300/0953—Gasifying agents
    • C10J2300/0959—Oxygen
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10J—PRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
    • C10J2300/00—Details of gasification processes
    • C10J2300/09—Details of the feed, e.g. feeding of spent catalyst, inert gas or halogens
    • C10J2300/0953—Gasifying agents
    • C10J2300/0973—Water
    • C10J2300/0976—Water as steam
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10J—PRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
    • C10J2300/00—Details of gasification processes
    • C10J2300/09—Details of the feed, e.g. feeding of spent catalyst, inert gas or halogens
    • C10J2300/0983—Additives
    • C10J2300/0996—Calcium-containing inorganic materials, e.g. lime

Definitions

  • This invention relates generally to a continuous process for the preparation of a mixture of carbon, monoxide and hydrogen gases.
  • a melter-gasifier is used in which fossil fuel and oxygen, as well as steam and lime or limestone, are fed to a pressurized molten metal bath to produce the mixture of carbon monoxide and hydrogen gases.
  • melter-gasifiers for effecting the partial combustion of the carbon content of fossil fuels in a molten metal bath to produce a gaseous mixture largely composed of hydrogen and carbon monoxide are well known in the art. Such melter-gasifiers are shown, for example, in U.S. Patents Nos. 3,533,739; 3,526,478 and 4,062,657.
  • melter-gasifier More recently it has been recognized that improved efficiency can be achieved in the operation of such a melter-gasifier if the conversion of the carbonaceous fossil fuel is carried out in a pressurized reaction system. However, if a pressurized system is used, the removal from the melter-gasifier of molten slag accumulating on the surface of the molten bath presents a problem. If the operation of the melter-gasifier is interrupted periodically to permit batchwise removal of the molten slag, there will be a discontinuous flow of product gases from the system.
  • shut-off valves at the top and bottom of the lock hopper which must maintain a tight seal on the pressurized systems, are exposed to a flood of water as the mixture of slag and water enters the hopper and is discharged therefrom. This water tends to wash away lubricants on the valve parts and to corrode them. Also large amounts of cooling water are used because the lock hopper is flooded and discharged during each operating cycle.
  • the objects and advantages of the present method are achieved in general by providing a system wherein the molten slag is continuously withdrawn from the melter- gasifier and delivered to a body of cooling water in a quenching chamber as described above, but the solidified slag is de-watered before being removed from the pressurized system through a pressure lock. As described below, the quantity of water used can be minimized by withdrawing quench water from the quench chamber and cooling and re-circulating it.
  • the numeral 10 designates a melter-gasifier reactor of conventional construction containing a molten iron bath 12 with a layer of slag 14 floating thereon.
  • a feed tube assembly 16 comprising an inner tube 18 and an outer tube 20.
  • a mixture of steam and oxygen from a suitable source is fed to the reactor through tube 18 and a mixture of powdered coal and limestone is fed through the tube 20.
  • Partial combustion of the coal in the presence of steam at the discharge ends of the tubes provides heat to maintain bath 12 and slag layer 14 molten and produces a gaseous mixture largely composed of carbon monoxide and hydrogen which may be withdrawn from the reactor through a discharge port 22.
  • the limestone promotes the formation of a fluid slag containing the residual ash from the combination of the coal and thus facilitates the removal of this residue from the reactor.
  • the reactor is desirably operated at an elevated pressure.
  • the fluid slag is continuously withdrawn from reactor 10 through a lateral passage 24 which connects the reactor with a quenching chamber 26 containing a body of water 28 for quenching the slag and converting it to solid granular form.
  • a quenching chamber 26 containing a body of water 28 for quenching the slag and converting it to solid granular form.
  • an oxygen lance 30 Located in the side wall of quench chamber 26 there is an oxygen lance 30 having its discharge end positioned in registry with a passage 24. The oxygen lance is useful in preventing blockage of passage 24 due to solidification of slag therein.
  • the mixture of granular slag and water in quench chamber 26 flows downwardly through discharge pipe 32 to the outlet end of a screw conveyor 34 which as shown in the drawing extends upwardly and outwardly from pipe 32.
  • a screw conveyor 34 which as shown in the drawing extends upwardly and outwardly from pipe 32.
  • the slag is transported by conveyor 34 to the upper end of a pressure lock generally designated 36 and the quench water flows through pipe 38 containing a back pressure valve 40 to a settling tank 42 wherein suspended solids are moved by sedimentation.
  • the clarified water is transferred by pump 44 through pipe 46 to the cooling tower 48 wherein it is cooled and thence by pump 50 through pipe 52 and branch pipes 54 and 56 back to the quenching chamber 26.
  • Make-up cooling water may be added to the cooling water circuit through pipe 58.
  • the pressure lock 36 may be of the general type disclosed in U.S. Patent No. 3,710,808. It comprises the hopper 60 and the double valve assemblies 62 and 64. At its upper end the conveyor 34 delivers granular slag to the accumulating hopper 66. From time to time the valves 62 are opened with the valves 64 closed to permit accumulated flag to flow from hopper 66 to hopper 60. Valves 62 are then closed and valves 64 opened to discharge the granular slag from the system.

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Combustion & Propulsion (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Carbon And Carbon Compounds (AREA)
  • Waste-Gas Treatment And Other Accessory Devices For Furnaces (AREA)
  • Gasification And Melting Of Waste (AREA)
EP84107105A 1983-06-20 1984-06-20 Verfahren zur Herstellung einer Mischung von Kohlenstoffmonoxyd und Wasserstoff und Schmelzbadvergaser Withdrawn EP0129256A3 (de)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
US50582683A 1983-06-20 1983-06-20
US505826 2000-02-17

Publications (2)

Publication Number Publication Date
EP0129256A2 true EP0129256A2 (de) 1984-12-27
EP0129256A3 EP0129256A3 (de) 1985-10-30

Family

ID=24012007

Family Applications (1)

Application Number Title Priority Date Filing Date
EP84107105A Withdrawn EP0129256A3 (de) 1983-06-20 1984-06-20 Verfahren zur Herstellung einer Mischung von Kohlenstoffmonoxyd und Wasserstoff und Schmelzbadvergaser

Country Status (3)

Country Link
EP (1) EP0129256A3 (de)
JP (1) JPS6011588A (de)
MX (1) MX164808B (de)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN110396435A (zh) * 2019-09-03 2019-11-01 牛强 一种双熔浴有机固废喷吹气化装置

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH03110053A (ja) * 1989-09-22 1991-05-10 Kobe Steel Ltd 連続鋳造設備における鋳片引抜ロールの制御方法

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB800812A (en) * 1955-04-15 1958-09-03 Kohlenscheidungs Gmbh Method and apparatus for the discharge of molten material from gas producers or the like
US3175566A (en) * 1963-09-05 1965-03-30 Koppers Co Inc Apparatus for removal by means of sluices of the gasification residues from spaces prevailing under increased pressure
DE2950865A1 (de) * 1979-12-18 1981-06-25 Klöckner-Humboldt-Deutz AG, 5000 Köln Vorrichtung zum vergasen von kohlenstoff und/oder kohlenstoffhaltigen medien
GB2078779A (en) * 1980-07-02 1982-01-13 Kloeckner Humboldt Deutz Ag Apparatus and method for production of reducing gases
GB2088892A (en) * 1980-12-01 1982-06-16 Sumitomo Metal Ind Process for Gasification of Solid Carbonaceous Material

Family Cites Families (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5821569B2 (ja) * 1974-09-06 1983-05-02 三菱重工業株式会社 コウブンシブツシツハイキブツネツブンカイソウチ
DE2829629C2 (de) * 1978-07-06 1982-07-29 Ruhrchemie Ag, 4200 Oberhausen Verfahren und Vorrichtung zum Ausschleusen von Rückständen aus dem Drucksystem einer Druckvergasungsanlage

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB800812A (en) * 1955-04-15 1958-09-03 Kohlenscheidungs Gmbh Method and apparatus for the discharge of molten material from gas producers or the like
US3175566A (en) * 1963-09-05 1965-03-30 Koppers Co Inc Apparatus for removal by means of sluices of the gasification residues from spaces prevailing under increased pressure
DE2950865A1 (de) * 1979-12-18 1981-06-25 Klöckner-Humboldt-Deutz AG, 5000 Köln Vorrichtung zum vergasen von kohlenstoff und/oder kohlenstoffhaltigen medien
GB2078779A (en) * 1980-07-02 1982-01-13 Kloeckner Humboldt Deutz Ag Apparatus and method for production of reducing gases
GB2088892A (en) * 1980-12-01 1982-06-16 Sumitomo Metal Ind Process for Gasification of Solid Carbonaceous Material

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN110396435A (zh) * 2019-09-03 2019-11-01 牛强 一种双熔浴有机固废喷吹气化装置
EP3808830A4 (de) * 2019-09-03 2021-10-06 Niu, Qiang Vergaser für organische feste abfälle durch einspritzen in ein bad aus eisenschmelze und schlacke
US11795407B2 (en) 2019-09-03 2023-10-24 Qiang Niu Gasifier for organic solid waste by injection into molten iron and slag bath

Also Published As

Publication number Publication date
EP0129256A3 (de) 1985-10-30
JPS6011588A (ja) 1985-01-21
MX164808B (es) 1992-09-25

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Effective date: 19870622

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18D Application deemed to be withdrawn

Effective date: 19871103

RIN1 Information on inventor provided before grant (corrected)

Inventor name: VIRAMONTES-BROWN, RICARDO

Inventor name: BERRUN-CASTANON, JORGE DOMINGO