EP0175207A2 - Process and apparatus for gasifying refuse - Google Patents

Process and apparatus for gasifying refuse Download PDF

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Publication number
EP0175207A2
EP0175207A2 EP85111104A EP85111104A EP0175207A2 EP 0175207 A2 EP0175207 A2 EP 0175207A2 EP 85111104 A EP85111104 A EP 85111104A EP 85111104 A EP85111104 A EP 85111104A EP 0175207 A2 EP0175207 A2 EP 0175207A2
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EP
European Patent Office
Prior art keywords
gas
waste
slag
openings
liquid
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.)
Granted
Application number
EP85111104A
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German (de)
French (fr)
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EP0175207B1 (en
EP0175207A3 (en
Inventor
Bernt Dr. Obkircher
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.)
Molten Metal Technology Inc
Original Assignee
Dornier System GmbH
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Publication date
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Priority to AT85111104T priority Critical patent/ATE39709T1/en
Publication of EP0175207A2 publication Critical patent/EP0175207A2/en
Publication of EP0175207A3 publication Critical patent/EP0175207A3/en
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Publication of EP0175207B1 publication Critical patent/EP0175207B1/en
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    • 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
    • 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
    • C10J3/72—Other features
    • C10J3/74—Construction of shells or jackets
    • 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
    • C10J2300/0913—Carbonaceous raw material
    • C10J2300/0946—Waste, e.g. MSW, tires, glass, tar sand, peat, paper, lignite, oil shale
    • 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
    • C10J2300/0956—Air or oxygen enriched air
    • 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
    • C10J2300/0983—Additives
    • C10J2300/0996—Calcium-containing inorganic materials, e.g. lime
    • 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
    • C10J2300/18—Details of the gasification process, e.g. loops, autothermal operation
    • C10J2300/1807—Recycle loops, e.g. gas, solids, heating medium, water
    • Y—GENERAL 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
    • Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10S—TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10S588/00—Hazardous or toxic waste destruction or containment
    • Y10S588/90—Apparatus

Definitions

  • the invention relates to a method and a device for the gasification of carbon-containing waste or organic special waste according to the preamble of claim 1.
  • PCB's polychlorinated biphenyls
  • HSH's hexachlorocyclohexanes
  • a process for the gasification of household waste (DE-OS 32 12 534) is known in which waste is introduced into a hot iron bath (approx. 1130 to 1600 ° C.) and an oxidizing agent is added.
  • the waste is first shredded to a particle size of at least 50 mm and added below the surface of the iron melt. Crushing is energy-intensive and - at least with toxic probe waste - dangerous.
  • the introduction of the waste under the molten iron is technically complex. In addition is not ensured that all waste particles really reach the temperature of the molten metal, which is necessary for the disposal of hazardous waste.
  • the object of the invention is to eliminate carbon-containing waste or organic hazardous waste economically and safely, the end products being intended to be harmless.
  • a device for carrying out the method is the subject of subclaims.
  • waste gasification with the addition of an oxidizing agent preferably air or oxygen
  • an oxidizing agent preferably air or oxygen
  • coal can also be added to the waste.
  • the gas formation lowers the level of the hot liquid in the first gas space and increases it in the second gas space. This continues until the gas reaches the upper edge of the openings or the upper, smaller openings in the partition between the two spaces of the reactor, flows through the openings, entrains slag or lets it flow through larger openings and the gas in the second reactor the liquid bubbles up and finally reaches the second gas space, where it is drawn off.
  • Iron is advantageously used as the liquid metal, then reactor temperatures of 1350 to 1400 ° C. are present in the iron bath.
  • oil poisons e.g. dioxins, PCB's, HCH's, warfare agents such as Tabun, Soman, Lost etc. even more safely
  • metals can be used which have even higher melting temperatures than iron, e.g. Chrome.
  • Metal alloys and melts of metal oxides can also be used to achieve the highest temperatures.
  • the incombustible slag-forming waste components float in liquid form on the liquid metal.
  • the reducing gases H 2 and CO possibly also H 2 0.
  • the sulfur, chlorine and fluorine impurities in the waste are initially in gaseous form as H 2 S, HC1, HF etc.
  • the slag is additionally supplied with lime from a corresponding container.
  • the gases mentioned are then unstable at the high temperatures and the presence of the basic slag, so that the impurities are present in the slag in the form of liquid CaS, CaCl 2 , CaF 2 etc.
  • the slag is constantly withdrawn from the reactor in liquid form, for example cooled by water.
  • the calcium compounds that leave the system through the slag discharge lock are completely water-insoluble and environmentally neutral and can be deposited as residue without any problems, while the product gas leaving the system only contains impurities in HC1, HF, H 2 S etc. in the ppm range.
  • the oxidizing agent can either be introduced directly into the hot liquid or blown into the first gas space above the liquid.
  • the method according to the invention can be operated batchwise or continuously.
  • a pressure lock in the first gas space is advantageous, as there is no pressure loss when the space is opened.
  • the opening can be so large that entire casks of poison can be introduced without prior crushing.
  • the process temperature can be increased by adding coal, preferably coal dust, or reduced by recycling process gas or by admixing water vapor or an inert gas. These gases can also be used to cool the oxidant injection nozzles.
  • the reactor is advantageously designed to be pressure-resistant, at least in the region of the first gas space, and has an upper region a pressure lock for the garbage and / or slag generator.
  • a pressure lock for the garbage and / or slag generator In the second gas space, one or more fume cupboards for gas and slag are provided. The height of the just opened fume cupboard in the second gas space depends on the liquid level.
  • the reactors used for the gasification are advantageously thermally insulated.
  • the waste or lime can be preheated with the heat of the product gases.
  • An electric heater can be provided for starting the process or as an additional heater.
  • the concentric arrangement of the two gas spaces in which e.g. the first gas space is encased by the second.
  • the first gas space then has practically no outer surface through which heat can escape.
  • the passage cross section of the openings in the partition between the two gas spaces should increase from top to bottom, so that the flow cross section that flows from one gas to the other has a disproportionately increasing flow cross section, the more the liquid level in the space from which the gas flows out decreases .
  • This can be done through larger or more openings in the lower part, also through openings whose cross-section is wider at the bottom than at the top, for example through triangular openings.
  • the increase in opening cross-section with increasing depth prevents vibrations of the two liquid columns.
  • the arrangement of the openings in the lower area automatically regulates the amount of gas that is transferred.
  • the size of the openings prevents unreacted waste components from passing through.
  • the height of the liquid column in the second room guarantees that the gases stay at the temperature of the hot liquid for longer.
  • Small openings on the lowered liquid level only allow small gas bubbles to pass through, which are then safely heated to the desired temperature in the liquid in the second gas space.
  • the smaller openings can be formed by porous ceramic stones or ceramic flow bodies with certain pore sizes, e.g. by 1 mm or less. Larger openings in the lower area of the lowered liquid allow easier passage of the liquid into the second gas space.
  • the invention is illustrated by a figure.
  • the figure shows schematically an apparatus for performing a method according to the invention.
  • a storage container 1 for waste is connected via a pressure lock 2 to a thermally insulated reactor 3, in which a liquid 4, here a liquid metal, is located.
  • An oxidizing agent 5 is blown into the liquid 4 via nozzles 6.
  • the reactor 3 contains two gas spaces 7 and 8, which are separated by a partition 9 with openings 9a in the lower region.
  • a reservoir 11 with lime is provided for converting the slag 10 floating on the metal.
  • a device known per se with slag cooling 12 slag discharge lock 13 and gas discharge 14 is provided for removing slag 10 and product gas a device known per se with slag cooling 12, slag discharge lock 13 and gas discharge 14 is provided.
  • the gas exhaust 14 is followed by a device 15 for heat recovery and dedusting.
  • the dust can be returned to the waste container 1 via a line 16.
  • Part of the product gas is fed through line 17 to a pump 18, which leads the gas to the nozzles 6 or to the pressure lock 2.
  • the other part of the product gas leaves the device
  • the pressure in the first gas space 7 rises and presses a part of the liquid 4 through the openings 9a into the second gas space 8. If the liquid level is pressed down to the uppermost opening 9a, slag 10 and product gas also reach the second gas space 8. It pearls Gas through the liquid 4 and takes on its temperature. The slag 10 and the product gas are drawn off at an opening at a suitable height in the second gas space.
  • the slag is preferably water-cooled and leaves the system through the slag discharge lock 13.
  • the product gas passes from the gas outlet 14 into a device 15 for heat recovery - gas cooling - and dedusting.
  • the resulting dust can be returned via line 16 to the waste storage container 1, while part of the gas via line 17 after corresponding compression with the pump 18 on the one hand for cooling the nozzles 6 for the oxidizing agent 5 and on the other hand for pressurizing the pressure lock 2 can be used at the entrance of the reactor 3.
  • the other part of the cleaned and cooled gas is discharged via line 19 for use, for example electricity and / or heat generation.
  • the heat generated in the waste heat device 15 can also be used to preheat the waste and lime feedstocks.

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

Abstract

Waste or refuse is fed to a first reaction chamber communicating with a second one through openings in the lower portion of a partition between the chambers and hot metal or the like is fed into at least one of the two chambers; gas is extracted from the second chamber and the pressure conditions are such that different liquid levels obtain in the two chambers causing reaction gas to bubble through the openings and the liquid in the second chamber. The principle product gases extracted are hydrogen, carbonoxide and inert gases. Lime is preferably added to the waste to be processed.

Description

Die Erfindung betrifft ein Verfahren und eine Vorrichtung zur Vergasung von kohlenstoffhaltigem Müll oder organischem Sondermüll nach dem Oberbegriff des Anspruchs 1.The invention relates to a method and a device for the gasification of carbon-containing waste or organic special waste according to the preamble of claim 1.

Allein schon wegen des Volumens stellen die anfallenden kommunalen und gewerblichen Müllmengen, die bisher hauptsächlich deponiert wurden, ein Problem dar. Deshalb ging man teilweise dazu über, den Müll zu verbrennen oder zu pyrolisieren.Because of the volume alone, the amount of municipal and commercial waste that has so far mainly been dumped is a problem. Therefore, some started to burn or pyrolyze the waste.

Bei der Müllverbrennung, die die Nutzung des Müllheizwertes (2 - 2,5 kWh/kg) erlaubt, entstehen jedoch hochagressive Gase (vor allem HC1, HF, SO2, NOx), die mit hohen Kosten aus dem Rauchgas wieder entfernt werden müssen, soweit dies überhaupt möglich ist.In waste incineration, which allows the use of the refuse calorific value (2 - 2.5 kWh / kg), highly aggressive gases (especially HC1, HF, SO 2 , NO x ) are produced, which have to be removed from the flue gas at high costs as far as this is possible at all.

Bei der Müllprolyse (Verschwelung des Mülls durch Wärmezufuhr unter Luftabschluß) ist dieses Problem auf die Verunreinigungen des entstehenden Schwelgases verlagert, in dem neben den erwünschten Gasen CH4, H2 und CO eine Vielzahl von lästigen Nebenprodukten wie H2S, HCl, HF, Teere, öle, Phenole und andere Kohlenwasserstoffe enthalten sind.In garbage prolysis (smoldering of the garbage through the supply of heat with the exclusion of air), this problem is shifted to the contamination of the smoldering gas formed, in which, in addition to the desired gases CH 4 , H 2 and CO, a large number of annoying by-products such as H 2 S, HCl, HF, Tars, oils, phenols and other hydrocarbons are included.

Diese Bestandteile müssen mit einer aufwendigen und daher teuren chemischen Verfahrenstechnik aus dem Schwelgas entfernt werden, bevor dies genutzt werden kann.These components must be removed from the carbonization gas using a complex and therefore expensive chemical process technology before this can be used.

Neben dem Problem der Müllbeseitigung existiert das Problem der Sondermüllbeseitigung. Vor allem Sondermüll aus organischen Verbindungen, polychlorierte Biphenyle (PCB's), Hexachlorcyclohexane (HCH's) Dioxin usw. können oft nur mit Schwierigkeiten sicher entsorgt oder vernichtet werden.In addition to the problem of waste disposal, there is the problem of hazardous waste disposal. Especially hazardous waste from organic compounds, polychlorinated biphenyls (PCB's), hexachlorocyclohexanes (HCH's) dioxin etc. can often only be disposed of safely or destroyed with difficulty.

Bekannt ist ein Verfahren zur Vergasung von Hausmüll (DE-OS 32 12 534), bei dem Müll in ein heißes Eisenbad (ca. 1130 bis 1600°C) eingebracht und ein Oxidationsmittel zugegeben wird. Bei diesem Verfahren wird der Müll vorher auf mindestens 50 mm Teilchengröße zerkleinert und unterhalb der Oberfläche der.Eisenschmelze zugegeben. Das Zerkleinern ist energieaufwendig und - zumindest bei giftigem Sondenmüll - gefährlich. Das Einbringen des Mülls unter die flüssige Eisenschmelze ist verfahrenstechnisch aufwendig. Zudem ist nicht gesichert, daß alle Müllpartikel wirklich die Temperatur der Metallschmelze erreichen, was bei der Sondermüllbeseitigung notwendig ist.A process for the gasification of household waste (DE-OS 32 12 534) is known in which waste is introduced into a hot iron bath (approx. 1130 to 1600 ° C.) and an oxidizing agent is added. In this process, the waste is first shredded to a particle size of at least 50 mm and added below the surface of the iron melt. Crushing is energy-intensive and - at least with toxic probe waste - dangerous. The introduction of the waste under the molten iron is technically complex. In addition is not ensured that all waste particles really reach the temperature of the molten metal, which is necessary for the disposal of hazardous waste.

Aufgabe der Erfindung ist es, kohlenstoffhaltigen Müll oder organischen Sondermüll wirtschaftlich und sicher zu beseitigen, wobei die Endprodukte ungefährlich sein sollen.The object of the invention is to eliminate carbon-containing waste or organic hazardous waste economically and safely, the end products being intended to be harmless.

Diese Aufgabe wird erfindungsgemäß durch ein Verfahren mit den in den Ansprüchen genannten Schritten gelöst.This object is achieved according to the invention by a method with the steps mentioned in the claims.

EineVorrichtung zur Durchführung des Verfahrens ist Gegenstand von Unteransprüchen.A device for carrying out the method is the subject of subclaims.

Erfindungsgemäß wird eine Müllvergasung unter Zugabe eines Oxidationsmittels,vorzugsweise Luft oder Sauerstoff, bei einer extrem hohen Temperatur (> 1000° C) in einem zweigeteilten Reaktor erreicht.According to the invention, waste gasification with the addition of an oxidizing agent, preferably air or oxygen, is achieved at an extremely high temperature (> 1000 ° C.) in a two-part reactor.

Die extrem hohe Temperatur ist in Reaktoren mit flüssigem Metallinhalt (z.B. Fe) garantiert. Wird Müll oder Sondermüll in einen solchen Reaktor eingebracht, zerfallen alle Kohlenwasserstoffe (C-H Verbindungen) und sonstigen organischen Verbindungen. Wasserstoff entweicht gasförmig, während Kohlenstoff im flüssigen Metall in Lösung geht. Dieser Kohlenstoff wird durch Einblasen eines Oxidationsmittels zu CO teiloxidiert und verläßt dadurch das flüssige Metall wieder, wie es vom Prinzip der Stahlherstellung aus Roheisen bekannt ist. Die brennbaren Bestandteile des Mülls verwandeln sich also in H2 und CO und erhöhen dadurch den Druck im ersten Gasraum des Reaktors. Die Oxidation von C zu CO ist exotherm und hält das flüssige Metall auf Temperatur, wenn nur der Reaktor gut genug thermisch isoliert ist. Dabei verbraucht sich dieses Metall im Laufe der Zeit nicht, sondern dient nur als Wärmeübertragungsmedium und Lösungsmittel für den Kohlenstoff.The extremely high temperature is guaranteed in reactors with a liquid metal content (eg Fe). If waste or special waste is placed in such a reactor, all hydrocarbons (CH compounds) and other organic compounds will disintegrate. Hydrogen escapes in gaseous form, while carbon dissolves in the liquid metal. This carbon is released by blowing an oxidation partially oxidized to CO and thereby leaves the liquid metal again, as is known from the principle of steel production from pig iron. The combustible constituents of the waste thus convert into H 2 and CO and thereby increase the pressure in the first gas space of the reactor. The oxidation of C to CO is exothermic and keeps the liquid metal at temperature if only the reactor is thermally insulated well enough. This metal does not wear out over time, but only serves as a heat transfer medium and solvent for the carbon.

Falls der Kohlenstoffgehalt des Mülls nicht ausreicht, die Temperatur der Schmelze aufrechtzuerhalten, kann dem Müll auch Kohle zugesetzt werden.If the carbon content of the waste is insufficient to maintain the temperature of the melt, coal can also be added to the waste.

Durch die Gasbildung wird der Spiegel der heißen Flüssigkeit im ersten Gasraum erniedrigt und im zweiten Gasraum erhöht. Dies geschieht so lange, bis das Gas den oberen Rand der öffnungen oder die oberen, kleineren öffnungen in der Trennwand zwischen den beiden Räumen des Reaktors erreicht, durch die Öffnungen hindurchströmt, Schlacke mitnimmt oder durch größere Öffnungen fließen läßt und das Gas im zweiten Reaktor durch die Flüssigkeit nach oben perlt und schließlich in den zweiten Gasraum gelangt, wo es abgezogen wird. Dadurch wird erfindungsgemäß garantiert, daß alle den Reaktor verlassenden Gase eine gewisse Zeit auf der Temperatur der Metallschmelze waren und bei vorteilhafter Wahl von Temperatur und Zeit sicher keine Kohlenwasserstoffe, das heißt Restbruchstücke des Mülls mehr enthalten.The gas formation lowers the level of the hot liquid in the first gas space and increases it in the second gas space. This continues until the gas reaches the upper edge of the openings or the upper, smaller openings in the partition between the two spaces of the reactor, flows through the openings, entrains slag or lets it flow through larger openings and the gas in the second reactor the liquid bubbles up and finally reaches the second gas space, where it is drawn off. This guarantees according to the invention that all the gases leaving the reactor have been at the temperature of the molten metal for a certain time and with an advantageous choice of Temperature and time certainly no hydrocarbons, that is, residual fragments of waste.

Als flüssiges Metall wird vorteilhaft Eisen verwendet, dann liegen im Eisenbad Reaktortemperaturen von 1350 bis 1400° C vor. Um speziell organischen Sondermüll, Ültragifte, zum Beispiel Dioxine, PCB's, HCH's, Kampfstoffe wie Tabun, Soman, Lost usw. noch sicherer zu zerstören, können Metalle verwendet werden, die noch höhere Schmelztemperaturen als Eisen aufweisen, wie z.B. Chrom. Ebenso sind Metallegierungen sowie Schmelzen von Metalloxiden zum Erreichen höchster Temperaturen verwendbar.Iron is advantageously used as the liquid metal, then reactor temperatures of 1350 to 1400 ° C. are present in the iron bath. In order to destroy organic hazardous waste, oil poisons, e.g. dioxins, PCB's, HCH's, warfare agents such as Tabun, Soman, Lost etc. even more safely, metals can be used which have even higher melting temperatures than iron, e.g. Chrome. Metal alloys and melts of metal oxides can also be used to achieve the highest temperatures.

Die unbrennbaren schlackebildenden Müllbestandteile schwimmen in flüssiger Form auf dem Flüssigmetall. Darüber befinden sich die reduzierenden Gase H2 und CO (eventuell auch H20). Die Schwefel-, Chlor- und Fluorverunreinigungen des Mülls liegen zunächst gasförmig als H2S, HC1, HF usw. vor.The incombustible slag-forming waste components float in liquid form on the liquid metal. Above are the reducing gases H 2 and CO (possibly also H 2 0). The sulfur, chlorine and fluorine impurities in the waste are initially in gaseous form as H 2 S, HC1, HF etc.

In einer vorteilhaften Ausführung des Verfahrens wird der Schlacke zusätzlich Kalk aus einem entsprechenden Behälter zugeführt. Die genannten Gase sind dann bei den hohen Temperaturen und der Anwesenheit der basischen Schlacke unstabil, so daß die Verunreinigungen, in Form von flüssigem CaS, CaCl2, CaF2 usw. in der Schlacke vorliegen. Die Schlacke wird dem Reaktor ständig flüssig entzogen und zum Beispiel mittels Wasser abgekühlt. Die Kalziumverbindungen, die durch die Schlackeaustrageschleuse das System verlassen, sind völlig wasserunlöslich und umweltneutral und können als Rückstand problemlos deponiert werden, während das das System verlassende Produktgas Verunreinigungen an HC1, HF, H2S usw. nur noch im ppm-Bereich enthält.In an advantageous embodiment of the method, the slag is additionally supplied with lime from a corresponding container. The gases mentioned are then unstable at the high temperatures and the presence of the basic slag, so that the impurities are present in the slag in the form of liquid CaS, CaCl 2 , CaF 2 etc. The slag is constantly withdrawn from the reactor in liquid form, for example cooled by water. The calcium compounds that leave the system through the slag discharge lock are completely water-insoluble and environmentally neutral and can be deposited as residue without any problems, while the product gas leaving the system only contains impurities in HC1, HF, H 2 S etc. in the ppm range.

Das Oxidationsmittel kann entweder direkt in die heiße Flüssigkeit eingegeben werden oder in den ersten Gasraum über der Flüssigkeit eingeblasen werden.The oxidizing agent can either be introduced directly into the hot liquid or blown into the first gas space above the liquid.

Das erfindungsgemäße Verfahren kann schubweise oder kontinuierlich betrieben werden. Im zweiten Fall ist eine Druckschleuse im ersten Gasraum vorteilhaft, durch die beim öffnen des Raumes kein Druckverlust entsteht. Die öffnung kann so groß sein, daß ganze Fässer mit Gift ohne vorherige Zerkleinerung eingebracht werden können. Die Prozeßtemperatur kann, je nach Kohlenstoffgehalt des Mülls, durch Zugabe von Kohle, vorzugsweise Kohlestaub, erhöht werden oder durch Rückführung von Prozeßgas oder durch Zumischen von Wasserdampf oder einem inerten Gas erniedrigt werden. Diese Gase können auch zum Kühlen der Einblasdüsen für das Oxidationsmittel verwendet werden.The method according to the invention can be operated batchwise or continuously. In the second case, a pressure lock in the first gas space is advantageous, as there is no pressure loss when the space is opened. The opening can be so large that entire casks of poison can be introduced without prior crushing. Depending on the carbon content of the waste, the process temperature can be increased by adding coal, preferably coal dust, or reduced by recycling process gas or by admixing water vapor or an inert gas. These gases can also be used to cool the oxidant injection nozzles.

Vorteilhaft ist der Reaktor, zumindest im Bereich des ersten Gasraumes,druckfest ausgebildet und weist im oberen Bereich eine Druckschleuse für den Müll und/oder Schlackebildner auf. Im zweiten Gasraum sind ein oder mehrere Abzüge für Gas und Schlacke vorgesehen. Die Höhe des gerade geöffneten Abzugs im zweiten Gasraum richtet sich nach dem Flüssigkeitsspiegel.The reactor is advantageously designed to be pressure-resistant, at least in the region of the first gas space, and has an upper region a pressure lock for the garbage and / or slag generator. In the second gas space, one or more fume cupboards for gas and slag are provided. The height of the just opened fume cupboard in the second gas space depends on the liquid level.

Vorteilhaft sind die für die Vergasung verwendeten Reaktoren thermisch isoliert. Zum Aufrechterhalten der Temperatur kann neben der Zuführung von Kohle eine Vorwärmung des Mülls oder des Kalks mit der Wärme der Produktgase erfolgen. Eine elektrische Heizung kann für den Start des Verfahrens oder als Zusatzheizung vorgesehen sein.The reactors used for the gasification are advantageously thermally insulated. In order to maintain the temperature, in addition to the supply of coal, the waste or lime can be preheated with the heat of the product gases. An electric heater can be provided for starting the process or as an additional heater.

Günstig ist auch die konzentrische Anordnung der zwei Gasräume, bei der z.B. der erste Gasraum vom zweiten umhüllt ist. Der erste Gasraum hat dann praktisch keine Außenfläche, durch die Wärme entweichen könnte.The concentric arrangement of the two gas spaces, in which e.g. the first gas space is encased by the second. The first gas space then has practically no outer surface through which heat can escape.

Vorteilhaft sollte der Durchlaßquerschnitt der Öffnungen in der Trennwand zwischen beiden Gasräumen von oben nach unten zunehmen, so daß das von einem in den anderen Raum strömende Gas einen überproportional anwachsenden Strömungsquerschnitt vorfindet, je mehr der Flüssigkeitsspiegel in dem Raum, aus dem das Gas ausströmt, absinkt. Dies kann durch größere oder mehr öffnungen im unteren Teil, auch auch durch Öffnungen erfolgen, deren Querschnitt unten breiter ist als oben, also z.B. durch dreieckige Öffnungen. Der Anstieg des Öffnungsquerschnitts mit zunehmender Tiefe verhindert Schwingungen der beiden Flüssigkeitssäulen.Advantageously, the passage cross section of the openings in the partition between the two gas spaces should increase from top to bottom, so that the flow cross section that flows from one gas to the other has a disproportionately increasing flow cross section, the more the liquid level in the space from which the gas flows out decreases . This can be done through larger or more openings in the lower part, also through openings whose cross-section is wider at the bottom than at the top, for example through triangular openings. The increase in opening cross-section with increasing depth prevents vibrations of the two liquid columns.

Die Anordnung der öffnungen im unteren Bereich regelt selbsttätig die Menge des übertretenden Gases. Die Größe der öffnungen verhindert ein Durchtreten von noch nicht reagierten Müllbestandteilen. Die Höhe der Flüssigkeitssäule im zweiten Raum garantiert einen längeren Aufenthalt der Gase auf der Temperatur der heißen Flüssigkeit.The arrangement of the openings in the lower area automatically regulates the amount of gas that is transferred. The size of the openings prevents unreacted waste components from passing through. The height of the liquid column in the second room guarantees that the gases stay at the temperature of the hot liquid for longer.

Kleine öffnungen am abgesenkten Flüssigkeitsspiegel lassen nur kleine Gasperlen übertreten, die dann in der Flüssigkeit im zweiten Gasraum sicher auf die gewünschte Temperatur erhitzt werden. Die kleineren Öffnungen können durch poröse Keramiksteine oder keramische Durchströmkörper mit bestimmten Porengrößen, z.B. um 1 mm oder kleiner, realisiert werden. Größere öffnungen im tieferen Bereich der abgesenkten Flüssigkeit erlauben ein leichteres Durchtreten der Flüssigkeit in den zweiten Gasraum.Small openings on the lowered liquid level only allow small gas bubbles to pass through, which are then safely heated to the desired temperature in the liquid in the second gas space. The smaller openings can be formed by porous ceramic stones or ceramic flow bodies with certain pore sizes, e.g. by 1 mm or less. Larger openings in the lower area of the lowered liquid allow easier passage of the liquid into the second gas space.

Das erfindungsgemäße Verfahren weist folgende Vorteile auf:

  • - Das Verfahren erlaubt eine relativ problemlose, d. h. sichere Vernichtung von kohlenstoffhaltigem Müll und Sondermüll, insbesondere von allen Rückständen aus der organischen Chemie wie z.B. alle chlorierten Kohlenwasserstoffe.
  • - Der Müll oder Sondermüll muß nicht in irgendeiner Weise vorbehandelt werden.
  • - Das Deponievolumen wird (ähnlich wie bei der Verbrennung und der Pyrolyse) drastisch reduziert.
  • - Der Brennwert des Mülls wird genutzt; das Metallbad bleibt auf der hohen Temperatur, bei Müll mit sehr wenig Kohlenstoffgehalt kann das entstehende Brenngas, H2 und CO, zum Nachheizen verwendet werden.
  • - Die Verunreinigungen im Müll fallen als völlig umweltneutrale, das heißt ungefährliche Stoffe an.
  • - Aufgrund der Einfachheit des Verfahrens können wirtschaftliche Vorteile gegenüber Müllverbrennung oder Müllpyrolyse erwartet werden.
The method according to the invention has the following advantages:
  • - The process allows a relatively problem-free, ie safe destruction of carbon-containing waste and special waste, in particular of all residues from organic chemistry such as all chlorinated hydrocarbons.
  • - The waste or special waste does not have to be pre-treated in any way.
  • - The landfill volume is reduced drastically (similar to incineration and pyrolysis).
  • - The calorific value of the waste is used; the metal bath remains at the high temperature, in the case of waste with very little carbon content, the fuel gas produced, H 2 and CO, can be used for reheating.
  • - The impurities in the garbage are completely environmentally neutral, that is, harmless substances.
  • - Due to the simplicity of the process, economic advantages over waste incineration or waste pyrolysis can be expected.

Die Erfindung wird anhand einer Figur näher erläutert.The invention is illustrated by a figure.

Die Figur zeigt schematisch eine Vorrichtung zur Durchführung eines erfindungsgemäßen Verfahrens.The figure shows schematically an apparatus for performing a method according to the invention.

Ein Vorratsbehälter 1 für Müll ist über eine Druckschleuse 2 mit einem thermisch isolierten Reaktor 3 verbunden, in dem sich eine Flüssigkeit 4, hier ein flüssiges Metall, befindet. Ein Oxidationsmittel 5 wird über Düsen 6 in die Flüssigkeit 4 eingeblasen. Der Reaktor 3 enthält zwei Gasräume 7 und 8, die durch eine Trennwand 9 mit öffnungen 9a im unteren Bereich getrennt sind. Zur Umwandlung der auf dem Metall schwimmenden Schlacke 10 ist ein Vorratsbehälter 11 mit Kalk vorgesehen. Zum Abziehen von Schlacke 10 und Produktgas ist eine an sich bekannte Vorrichtung mit Schlackenkühlung 12, Schlackenaustragschleuse 13 und Gasabzug 14 vorgesehen. Dem Gasabzug 14 schließt sich eine Vorrichtung 15 zur Abhitzenutzung und Entstaubung an. Der Staub kann über eine Leitung 16 in den Vorratsbehälter 1 für Müll zurückgeführt werden. Ein Teil des Produktgases wird durch die Leitung 17 einer Pumpe 18 zugeführt, die das Gas zu den Düsen 6 oder zu der Druckschleuse 2 führt. Der andere Teil des Produktgases verläßt die Vorrichtung 15 über die Leitung 19 zur weiteren Verwertung.A storage container 1 for waste is connected via a pressure lock 2 to a thermally insulated reactor 3, in which a liquid 4, here a liquid metal, is located. An oxidizing agent 5 is blown into the liquid 4 via nozzles 6. The reactor 3 contains two gas spaces 7 and 8, which are separated by a partition 9 with openings 9a in the lower region. A reservoir 11 with lime is provided for converting the slag 10 floating on the metal. For removing slag 10 and product gas a device known per se with slag cooling 12, slag discharge lock 13 and gas discharge 14 is provided. The gas exhaust 14 is followed by a device 15 for heat recovery and dedusting. The dust can be returned to the waste container 1 via a line 16. Part of the product gas is fed through line 17 to a pump 18, which leads the gas to the nozzles 6 or to the pressure lock 2. The other part of the product gas leaves the device 15 via the line 19 for further use.

Erfindungsgemäß wird der Müll wie folgt behandelt:

  • Aus dem Vorratsbehälter 1 gelangt der Müll grobstückig oder in ganzen Fässern in die Druckschleuse 2 am Eingang des ersten Gasraums 7 in den Reaktor 3. Der Müll fällt in die heiße Flüssigkeit 4. Die brennbaren Bestandteile zerfallen in Wasserstoff und Kohlenstoff. Die unbrennbaren schlackebildenden Bestandteile schwimmen als Schlacke 10 auf der Flüssigkeit 4. Durch die Düsen 6 wird ein Oxidationsmittel 5 eingeblasen. Der in der Flüssigkeit 4 gelöste Kohlenstoff wird zu CO teiloxidiert.
According to the waste is treated as follows:
  • The garbage reaches the pressure lock 2 at the entrance of the first gas space 7 into the reactor 3 in bulk or in whole drums from the storage container 1. The garbage falls into the hot liquid 4. The combustible components break down into hydrogen and carbon. The incombustible slag-forming constituents float as slag 10 on the liquid 4. An oxidizing agent 5 is blown in through the nozzles 6. The carbon dissolved in the liquid 4 is partially oxidized to CO.

Bei dieser Reaktion steigt der Druck in dem ersten Gasraum 7 und drückt einen Teil der Flüssigkeit 4 durch die öffnungen 9a in den zweiten Gasraum 8. Ist der Flüssigkeitsspiegel bis zur obersten Öffnung 9a herabgedrückt, gelangt auch Schlacke 10 und Produktgas in den zweiten Gasraum 8. Dabei perlt das Gas durch die Flüssigkeit 4 und nimmt dessen Temperatur an. Die Schlacke 10 und das Produktgas werden an einer in geeigneter Höhe angebrachten öffnung im zweiten Gasraum abgezogen. Die Schlacke wird vorzugsweise mit Wassergekühlt und verläßt das System durch die Schlackenaustragschleuse 13.During this reaction, the pressure in the first gas space 7 rises and presses a part of the liquid 4 through the openings 9a into the second gas space 8. If the liquid level is pressed down to the uppermost opening 9a, slag 10 and product gas also reach the second gas space 8. It pearls Gas through the liquid 4 and takes on its temperature. The slag 10 and the product gas are drawn off at an opening at a suitable height in the second gas space. The slag is preferably water-cooled and leaves the system through the slag discharge lock 13.

Das Produktgas gelangt vom Gasabzug 14 in eine Vorrichtung 15 zur Abhitzenutzung - Gaskühlung - und Entstaubung. Der dabei anfallende Staub kann über die Leitung 16 in den Müllvorratsbehälter 1 zurückgeführt werden, während ein Teil des Gases über die Leitung 17 nach entsprechender Kompression mit der Pumpe 18 einerseits zur Kühlung der Düsen 6 für das Oxidationsmittel 5 und andererseits zur Druckbeaufschlagung für die Druckschleuse 2 am Eingang des Reaktors 3 verwendet werden kann. Der andere Teil des gereinigten und gekühlten Gases wird über die Leitung 19 zur Nutzung, zum Beispiel Strom- und/oder Wärmeerzeugung abgeführt. Die in der Abhitzevorrichtung 15 anfallende Wärme kann noch zur Vorwärmung der Einsatzstoffe Müll und Kalk genutzt werden.The product gas passes from the gas outlet 14 into a device 15 for heat recovery - gas cooling - and dedusting. The resulting dust can be returned via line 16 to the waste storage container 1, while part of the gas via line 17 after corresponding compression with the pump 18 on the one hand for cooling the nozzles 6 for the oxidizing agent 5 and on the other hand for pressurizing the pressure lock 2 can be used at the entrance of the reactor 3. The other part of the cleaned and cooled gas is discharged via line 19 for use, for example electricity and / or heat generation. The heat generated in the waste heat device 15 can also be used to preheat the waste and lime feedstocks.

Claims (17)

1. Verfahren zur Vergasung von kohlenstoffhaltigem Müll oder organischem Sondermüll, wobei der Müll in eine heiße Flüssigkeit (4) mit einer Temperatur > 1000° C eingebracht wird und ein Oxidationsmittel (5) zugegeben wird, dadurch gekennzeichnet, daß eine im unteren Bereich mit Öffnungen (9a) versehene Trennwand (9) vorgesehen ist, die zwei Gasräume (7, 8) über der heißen Flüssigkeit (4) schafft, daß der Müll in den ersten Gasraum (7) eingebracht wird und daß die entstehenden Produktgase (hauptsächlich H21 CO und Inertgase) zusammen mit der Schlacke (10) im zweiten Gasraum (8) abgezogen werden.1. A process for the gasification of carbon-containing waste or organic special waste, the waste being introduced into a hot liquid (4) with a temperature> 1000 ° C and an oxidizing agent (5) being added, characterized in that one in the lower area with openings (9a) provided partition (9) is provided, which creates two gas spaces (7, 8) above the hot liquid (4), that the waste is introduced into the first gas space (7) and that the resulting product gases (mainly H 21 CO and inert gases) are drawn off together with the slag (10) in the second gas space (8). 2. Verfahren nach Anspruch 1, dadurch gekennzeichnet, daß das Oxidationsmittel (5) in die heiße Flüssigkeit (4) und/oder in den ersten Gasraum (7) eingeblasen wird.2. The method according to claim 1, characterized in that the oxidizing agent (5) in the hot liquid (4) and / or in the first gas space (7) is blown. 3. Verfahren nach Anspruch 1 oder 2, dadurch gekennzeichnet, daß das Einbringen des Mülls, der auch grobstückig sein kann, von der Seite oder von oben durch eine Druckschleuse (2) erfolgt, in der die Druckerhöhung durch rückgeführtes Produktgas erfolgen kann.3. The method according to claim 1 or 2, characterized in that the introduction of the garbage, which can also be coarse, from the side or from above through a pressure lock (2), in which the pressure increase can be carried out by recirculated product gas. 4. Verfahren nach einem der vorhergehenden Ansprüche, dadurch gekennzeichnet, daß zusätzlich der Schlacke (10) auf der heißen Flüssigkeit (4) ein Schlackebildner wie Kalk (CaO, 11) zugeführt wird, um aus den entstehenden Gasen HC1, HF, H2S und sonstige Verunreinigungen zu entfernen, und die Schlacke (10) flüssig abgezogen und abgekühlt wird.4. The method according to any one of the preceding claims, characterized in that in addition the slag (10) on the hot liquid (4) a slag generator such as lime (CaO, 11) is supplied to the resulting gases HC1, HF, H 2 S and to remove other impurities, and the slag (10) is drawn off in liquid form and cooled. 5. Verfahren nach einem der vorhergehenden Ansprüche, dadurch gekennzeichnet, daß als heiße Flüssigkeit (4) eine Metallschmelze aus einem oder mehreren der Metalle: Fe, Co, Ni, Cr oder Mn verwendet wird.5. The method according to any one of the preceding claims, characterized in that a metal melt of one or more of the metals: Fe, Co, Ni, Cr or Mn is used as the hot liquid (4). 6. Verfahren nach einem der vorhergehenden Ansprüche, dadurch gekennzeichnet, daß zur Erreichung extremer Temperaturen als heiße Flüssigkeit (4) eine Metalloxidschmelze wie Kupferoxid verwendet wird.6. The method according to any one of the preceding claims, characterized in that a metal oxide melt such as copper oxide is used as hot liquid (4) to achieve extreme temperatures. 7. Verfahren nach einem der vorhergehenden Ansprüche, dadurch gekennzeichnet, daß als Oxidationsmittel (5) Sauerstoff oder Luft verwendet wird.7. The method according to any one of the preceding claims, characterized in that oxygen or air is used as the oxidizing agent (5). 8. Verfahren nach einem der vorhergehenden Ansprüche, dadurch gekennzeichnet, daß zur Regelung der Temperatur in der heißen Flüssigkeit (4) und zur Kühlung der Düsen (6) ein Teil des Produktgases nach Entstaubung und Abkühlung oder ein anderes Gas wie Wasserdampf zusammen mit dem Oxidationsmittel (5) in die Flüssigkeit (4) oder den Raum (7) darüber eingeblasen wird.8. The method according to any one of the preceding claims, characterized in that for controlling the temperature in the hot liquid (4) and for cooling the nozzles (6), part of the product gas after dedusting and cooling or another gas such as water vapor together with the oxidizing agent (5) is blown into the liquid (4) or the space (7) above it. 9. Verfahren nach einem der vorhergehenden Ansprüche, dadurch gekennzeichnet, daß den Müllsorten, die einen geringen Brennwert besitzen oder einen zu geringen Kohlenstoffgehalt aufweisen, Kohle- vorzugsweise staubförmig - zugesetzt wird.9. The method according to any one of the preceding claims, characterized in that the garbage types, which have a low calorific value or have too low a carbon content, coal - preferably dusty - is added. 10. Verfahren nach einem der vorhergehenden Ansprüche, dadurch gekennzeichnet, daß der Wärmeinhalt der Produktgase zur Vorwärmung der Einsatzstoffe Müll und/oder Kalk (11) verwendet wird.10. The method according to any one of the preceding claims, characterized in that the heat content of the product gases for preheating the input materials waste and / or lime (11) is used. 11. Vorrichtung zur Durchführung des Verfahrens eines der vorhergehenden Ansprüche, dadurch gekennzeichnet, daß der erste Gasraum (7) druckfest ausgebildet ist und oberhalb der Flüssigkeit (4) eine Druckschleuse (2) für Müll und/oder Schlackebildner enthält und daß der zweite Gasraum (8) einen oder mehrere in verschiedenen Höhen angebrachte Abzüge für Produktgas und Schlacke (10) enthält.11. Device for performing the method of one of the preceding claims, characterized in that the first gas space (7) is designed to be pressure-resistant and above the liquid (4) contains a pressure lock (2) for waste and / or slag formers and in that the second gas space ( 8) contains one or more fume cupboards (10) for product gas and slag. 12. Vorrichtung nach Anspruch 11, dadurch gekennzeichnet, daß die beiden Gasräume (7, 8) thermisch isoliert sind und/oder eine elektrische Widerstands- oder Induktionsheizung vorgesehen ist.12. The apparatus according to claim 11, characterized in that the two gas spaces (7, 8) are thermally insulated and / or an electrical resistance or induction heating is provided. 13. Vorrichtung nach Anspruch 11 oder 12, dadurch gekennzeichnet, daß ein Gasraum den anderen Gasraum konzentrisch umschließt.13. The apparatus of claim 11 or 12, characterized in that a gas space concentrically surrounds the other gas space. 14. Vorrichtung nach einem der Ansprüche 11 bis 13, dadurch gekennzeichnet, daß der Durchlaßquerschnitt der Öffnungen (9a) in der Trennwand (9) zwischen beiden Gasräumen (7, 8) von oben nach unten zunimmt.14. Device according to one of claims 11 to 13, characterized in that the passage cross section of the openings (9a) in the partition (9) between the two gas spaces (7, 8) increases from top to bottom. 15. Vorrichtung nach Anspruch 14, dadurch gekennzeichnet, daß im unteren Teil der Trennwand (9) größere oder mehr öffnungen (9a) vorhanden sind als im oberen Teil.15. The apparatus according to claim 14, characterized in that in the lower part of the partition (9) larger or more openings (9a) are present than in the upper part. 16. Vorrichtung nach Anspruch 14, dadurch gekennzeichnet, daß die öffnungen (9a) oben schmäler sind als unten, vorzugsweise Dreiecksform aufweisen und/oder in den oberen Enden der öffnungen (9a) poröse keramische Durchströmkörper mit definierter Porengröße angeordnet sind.16. The apparatus according to claim 14, characterized in that the openings (9a) are narrower at the top than at the bottom, preferably triangular in shape and / or in the upper ends of the openings (9a) porous ceramic flow bodies are arranged with a defined pore size. 17. Vorrichtung nach Anspruch 16, dadurch gekennzeichnet, daß die Poren in der Größenordnung von 1 mm und/oder darunter liegen.17. The apparatus according to claim 16, characterized in that the pores are in the order of 1 mm and / or below.
EP85111104A 1984-09-15 1985-09-03 Process and apparatus for gasifying refuse Expired EP0175207B1 (en)

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Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0464802A1 (en) * 1990-07-03 1992-01-08 Franz Puschauer Process for the production of synthetic power gas by a material melting bath process
WO1993025278A1 (en) * 1992-06-08 1993-12-23 Molten Metal Technology, Inc. Method and appartus for treating organic waste
WO1993025277A1 (en) * 1992-06-08 1993-12-23 Molten Metal Technology, Inc. Method for treating organic waste
US5537940A (en) * 1993-06-08 1996-07-23 Molten Metal Technology, Inc. Method for treating organic waste
EP0897967A2 (en) * 1997-08-13 1999-02-24 LINDE-KCA-Dresden GmbH Process and apparatus for gasifying waste materials
WO2001040411A1 (en) * 1999-12-03 2001-06-07 Agriculture Azote Et Carbone Organiques Method and installation for gasifying carbonaceous compounds

Families Citing this family (39)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE3608005A1 (en) * 1986-03-11 1987-10-01 Dornier System Gmbh Process for disposing of special waste
CA2037860C (en) * 1990-03-08 2001-07-31 Paul Katona Waste processing
US5776420A (en) * 1991-07-29 1998-07-07 Molten Metal Technology, Inc. Apparatus for treating a gas formed from a waste in a molten metal bath
US5585532A (en) * 1991-07-29 1996-12-17 Molten Metal Technology, Inc. Method for treating a gas formed from a waste in a molten metal bath
BR9206400A (en) * 1991-07-29 1994-12-27 Molten Metal Tech Inc Method and system for converting a feed product to a dissolved atomic constituent
US5354940A (en) * 1991-07-29 1994-10-11 Molten Metal Technology, Inc. Method for controlling chemical reaction in a molten metal bath
US5191154A (en) * 1991-07-29 1993-03-02 Molten Metal Technology, Inc. Method and system for controlling chemical reaction in a molten bath
RU2114356C1 (en) * 1991-12-06 1998-06-27 Текнолоджикал Рисорсиз ПТИ Лимитед Method of destruction of organic wastes
US5435814A (en) * 1992-08-13 1995-07-25 Ashland Inc. Molten metal decomposition apparatus
US5645615A (en) * 1992-08-13 1997-07-08 Ashland Inc. Molten decomposition apparatus and process
DE4333082A1 (en) * 1992-10-10 1994-04-14 Heinz Hinterholzinger Fuel gas prodn from esp domestic waste - by reaction with coal and water in abandoned coal mine.
US5744117A (en) * 1993-04-12 1998-04-28 Molten Metal Technology, Inc. Feed processing employing dispersed molten droplets
AT401301B (en) * 1993-07-01 1996-08-26 Holderbank Financ Glarus REACTOR AND METHOD FOR MELTING COMBUSTION RESIDUES
AUPN226095A0 (en) * 1995-04-07 1995-05-04 Technological Resources Pty Limited A method of producing metals and metal alloys
US6432149B1 (en) * 1995-06-02 2002-08-13 Marathon Ashland Petroleum Llc Burner-feed multi-zone molten metal syngas generator
DE19622152A1 (en) * 1996-06-01 1997-12-04 Krupp Uhde Gmbh Process for the production of gas
DE19629544C2 (en) * 1996-07-22 1998-10-22 Linde Kca Dresden Gmbh Process for the preparation of polyvinyl chloride (PVC) and use of the process
AUPO426096A0 (en) 1996-12-18 1997-01-23 Technological Resources Pty Limited Method and apparatus for producing metals and metal alloys
AUPO426396A0 (en) 1996-12-18 1997-01-23 Technological Resources Pty Limited A method of producing iron
AUPO944697A0 (en) * 1997-09-26 1997-10-16 Technological Resources Pty Limited A method of producing metals and metal alloys
AUPP442598A0 (en) 1998-07-01 1998-07-23 Technological Resources Pty Limited Direct smelting vessel
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MY119760A (en) 1998-07-24 2005-07-29 Tech Resources Pty Ltd A direct smelting process
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AUPQ365799A0 (en) 1999-10-26 1999-11-18 Technological Resources Pty Limited A direct smelting apparatus and process
US6602321B2 (en) 2000-09-26 2003-08-05 Technological Resources Pty. Ltd. Direct smelting process
US6717026B2 (en) * 2001-02-27 2004-04-06 Clean Technologies International Corporation Molten metal reactor utilizing molten metal flow for feed material and reaction product entrapment
TW200711030A (en) 2005-02-23 2007-03-16 Kyocera Corp Joined article and member for holding wafer and structure for mounting the same, and method for treating wafer
JP5327417B2 (en) * 2006-04-12 2013-10-30 株式会社Ｉｈｉ Fluidized bed reactor
US8303916B2 (en) * 2008-02-01 2012-11-06 Oscura, Inc. Gaseous transfer in multiple metal bath reactors

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR2186524A1 (en) * 1972-05-30 1974-01-11 Siderurgie Fse Inst Rech Continuous reducing gas prodn - by injecting hydrocarbon and oxygen into different parts of an agitated molten metal bath
DE2304369B1 (en) * 1973-01-26 1974-05-09 Mannesmann Ag, 4000 Duesseldorf Method and device for the pyrolytic build-up of waste materials
US4244180A (en) * 1979-03-16 1981-01-13 Rasor Associates, Inc. Process for producing fuel gases from carbonaceous material

Family Cites Families (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
NL45687C (en) * 1934-10-30
DE706304C (en) * 1939-04-09 1941-05-23 Gewerkschaft Ver Klosterbusch Process for the production of gases, especially water gas, and gas generators for carrying out the process
US2612444A (en) * 1948-12-28 1952-09-30 Rummel Roman Production of metals from their ores
DE940132C (en) * 1953-02-03 1956-03-08 Otto & Co Gmbh Dr C Gas generator with slag bath and process for its operation
US3252773A (en) * 1962-06-11 1966-05-24 Pullman Inc Gasification of carbonaceous fuels
US3916617A (en) * 1974-03-29 1975-11-04 Rockwell International Corp Process for production of low BTU gas
US4187672A (en) * 1977-11-17 1980-02-12 Rasor Associates, Inc. Apparatus for converting carbonaceous material into fuel gases and the recovery of energy therefrom
DE2813207A1 (en) * 1978-03-25 1979-10-04 Bosch Gmbh Robert SYSTEM FOR CORRECTION OF SIGNALS THAT ARE TAKEN FREQUENCY MODULATED FROM A RECORDING MEDIA
DE2813209A1 (en) * 1978-03-25 1979-10-04 Kloeckner Humboldt Deutz Ag Gasification of solid fuels in molten copper bath - with removal of sulphur by reaction with the copper
US4362554A (en) * 1981-03-06 1982-12-07 Skf Steel Engineering Aktiebolag Method and apparatus for manufacturing sponge iron
DE3111168C2 (en) * 1981-03-21 1987-01-08 Klöckner-Humboldt-Deutz AG, 5000 Köln Process and apparatus for producing a gas containing essentially H↓2↓ and CO
DE3212534A1 (en) * 1982-02-27 1983-10-13 Artur Richard 6000 Frankfurt Greul Process and equipment for gasifying domestic and similar refuse

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR2186524A1 (en) * 1972-05-30 1974-01-11 Siderurgie Fse Inst Rech Continuous reducing gas prodn - by injecting hydrocarbon and oxygen into different parts of an agitated molten metal bath
DE2304369B1 (en) * 1973-01-26 1974-05-09 Mannesmann Ag, 4000 Duesseldorf Method and device for the pyrolytic build-up of waste materials
US4244180A (en) * 1979-03-16 1981-01-13 Rasor Associates, Inc. Process for producing fuel gases from carbonaceous material

Cited By (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0464802A1 (en) * 1990-07-03 1992-01-08 Franz Puschauer Process for the production of synthetic power gas by a material melting bath process
WO1993025278A1 (en) * 1992-06-08 1993-12-23 Molten Metal Technology, Inc. Method and appartus for treating organic waste
WO1993025277A1 (en) * 1992-06-08 1993-12-23 Molten Metal Technology, Inc. Method for treating organic waste
US5537940A (en) * 1993-06-08 1996-07-23 Molten Metal Technology, Inc. Method for treating organic waste
EP0897967A2 (en) * 1997-08-13 1999-02-24 LINDE-KCA-Dresden GmbH Process and apparatus for gasifying waste materials
EP0897967A3 (en) * 1997-08-13 1999-03-24 LINDE-KCA-Dresden GmbH Process and apparatus for gasifying waste materials
WO2001040411A1 (en) * 1999-12-03 2001-06-07 Agriculture Azote Et Carbone Organiques Method and installation for gasifying carbonaceous compounds
FR2801895A1 (en) * 1999-12-03 2001-06-08 Agriculture Azote Et Carbone O METHOD AND INSTALLATION FOR GASIFYING CARBON COMPOUNDS
US7087098B2 (en) 1999-12-03 2006-08-08 Agriculture Azote Et Carbone Organiques Method and installation for gasifying carbonaceous compounds

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EP0175207B1 (en) 1989-01-04
ATE39709T1 (en) 1989-01-15
EP0175207A3 (en) 1986-12-30
US4681599A (en) 1987-07-21
DE3434004A1 (en) 1986-05-22
DE3434004C2 (en) 1987-03-26
JPS61133187A (en) 1986-06-20

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