EP1133539A1 - Reactor for gasifying granular fuels that form a fixed bed - Google Patents

Reactor for gasifying granular fuels that form a fixed bed

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Publication number
EP1133539A1
EP1133539A1 EP99947283A EP99947283A EP1133539A1 EP 1133539 A1 EP1133539 A1 EP 1133539A1 EP 99947283 A EP99947283 A EP 99947283A EP 99947283 A EP99947283 A EP 99947283A EP 1133539 A1 EP1133539 A1 EP 1133539A1
Authority
EP
European Patent Office
Prior art keywords
reactor
fixed bed
product gas
separator
ring wall
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
EP99947283A
Other languages
German (de)
French (fr)
Other versions
EP1133539B1 (en
Inventor
Gerhard Schmitt
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.)
MG Technologies AG
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MG Technologies AG
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Filing date
Publication date
Application filed by MG Technologies AG filed Critical MG Technologies AG
Publication of EP1133539A1 publication Critical patent/EP1133539A1/en
Application granted granted Critical
Publication of EP1133539B1 publication Critical patent/EP1133539B1/en
Anticipated expiration legal-status Critical
Expired - Lifetime 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
    • C10J3/72—Other features
    • C10J3/82—Gas withdrawal means
    • C10J3/84—Gas withdrawal means with means for removing dust or tar from the gas
    • 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
    • C10J3/02—Fixed-bed gasification of lump fuel
    • 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
    • C10J3/02—Fixed-bed gasification of lump fuel
    • C10J3/20—Apparatus; Plants
    • 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
    • C10J3/02—Fixed-bed gasification of lump fuel
    • C10J3/20—Apparatus; Plants
    • C10J3/34—Grates; Mechanical ash-removing devices
    • C10J3/40—Movable grates
    • C10J3/42—Rotary grates
    • 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
    • C10J3/82—Gas withdrawal means
    • 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
    • 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
    • C10K1/02—Dust removal
    • C10K1/026—Dust removal by centrifugal forces
    • 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

Definitions

  • the invention relates to a reactor for gasifying granular fuels, the fuel forming a fixed bed in the reactor, into the lower region of which oxygen-containing gasifying agent is introduced, which moves upwards in the fixed bed, and wherein product gas containing hydrogen and carbon oxides is removed above the fixed bed through a discharge duct from the Discharges reactor.
  • the invention is based on the object of designing the reactor mentioned at the outset in such a way that even in the case of a strong product gas stream, no disruptive amounts of fine-grained fuel are drawn off from the reactor.
  • This is achieved according to the invention in that at least one centrifugal separator for separating solids from the product gas is arranged in the reactor, which has an inlet opening for dust-containing product gas coming from the fixed bed, an outlet line for product gas and a solid discharge line leading into the fixed bed, the outlet line with the discharge channel of the reactor is connected.
  • centrifugal separators are arranged in the reactor, the outlet lines of the separators in one in the upper region of the reactor arranged annular chamber open, which is connected to the discharge channel.
  • An expedient development of the invention consists in that a vertical ring wall is arranged in the upper area of the reactor and that the inlet opening of the separator is located outside the reactor area enclosed by the ring wall.
  • the ring wall ensures that the inlet opening of the separator is above the fixed bed.
  • the reactors usually operate at pressures from 1 to 80 bar.
  • Fig. 1 shows a gasification reactor with a rotating grate in
  • FIG. 2 shows a second reactor variant in the representation analogous to FIG. 2 and FIG. 3 a further reactor variant.
  • the reactor of FIG. 1 has a housing (1) which is usually water-cooled.
  • the granular fuel comes from a storage container (2) and falls through the then opened valve (3) onto the fixed bed (4).
  • a rotating grate (5) In the lower area of the reactor there is a rotating grate (5), which is mixed with a gasification medium line (6) Feeds oxygen and water vapor, which is distributed from the rotating grate (5) into the fixed bed (4). In a manner not shown, ash is drawn down through the opening (7).
  • a vertical ring wall (10) is connected to the reactor housing (1) in a gas-tight manner at the upper end and serves as a boundary for an annular chamber (11) which is connected to the discharge channel (9).
  • a horizontal partition (12) is arranged in the form of an annular disc between the housing (1) and the annular wall (10) as the lower boundary of the annular chamber (11).
  • Fig. 1 two cyclones (13) are shown, the outlet lines (14) lead upwards into the annular chamber (11).
  • the inlet opening (15) of each cyclone (13) is located below the partition (12) and above the fixed bed (4). Dust-containing product gas, which flows out of the fixed bed (4), forcibly enters through the openings (15) into one of the two cyclones (13), with the separated solids being discharged through the respective solid matter discharge line (16) back into the fixed bed (4) become.
  • the lower area of the discharge line (16) is widened for better drainage of the solids downwards.
  • the number of cyclones can be chosen arbitrarily, it will usually be 1 to 10.
  • the product gas, which leaves the cyclones (13) flows through the outlet lines (14) first into the annular chamber (11) and then to the exhaust duct (9). The dust content of this product gas is limited in this way, so that malfunctions are avoided.
  • the cyclones (13) are within the area enclosed by the ring wall (10) and thus more or less in the fixed bed (4), where the temperatures are relatively low.
  • the cyclones (13) are located outside the ring wall (10) and the product gas flows around them.
  • the reference numerals of FIG. 2 have the meaning already explained together with FIG. 1.
  • a gasification reactor with a rotating grate (5) can easily be equipped with only a cyclone (13) according to Fig. 3, and also the reactor of Fig. 3, the trigger more fluid Slag works, have several separating cyclones (13), as was explained together with FIG. 1 or FIG. 2.

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Combustion & Propulsion (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Organic Chemistry (AREA)
  • Mechanical Engineering (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Devices And Processes Conducted In The Presence Of Fluids And Solid Particles (AREA)
  • Processing Of Solid Wastes (AREA)
  • Gas Separation By Absorption (AREA)
  • Cyclones (AREA)

Abstract

The inventive reactor contains a fixed bed into whose lower area an oxygen-containing gasifying agent is introduced. Said gasifying agent moves upwards in the fixed bed. Product gas containing hydrogen and carbon monoxide is guided out of the reactor over the fixed bed, through a discharge channel. At least one cyclone is located in the reactor for separating solids from the product gas. Said cyclone has an inlet for the dust-laden product gas coming from the fixed bed, a discharge line for product gas and a solids removal line leading into the fixed bed. Said cyclone discharge line is connected to the discharge channel of the reactor.

Description

Reaktor zum Vergasen körniger Brennstoffe, die ein Festbett bildenReactor for gasifying granular fuels that form a fixed bed
Beschreibungdescription
Die Erfindung betrifft einen Reaktor zum Vergasen körniger Brennstoffe, wobei der Brennstoff im Reaktor ein Festbett bildet, in dessen unteren Bereich Sauerstoffhaltiges Vergasungsmittel eingeleitet wird, das sich im Festbett aufwärts bewegt und wobei man Wasserstoff und Kohlenoxide enthaltendes Produktgas über dem Festbett durch einen Abzugskanal aus dem Reaktor abführt .The invention relates to a reactor for gasifying granular fuels, the fuel forming a fixed bed in the reactor, into the lower region of which oxygen-containing gasifying agent is introduced, which moves upwards in the fixed bed, and wherein product gas containing hydrogen and carbon oxides is removed above the fixed bed through a discharge duct from the Discharges reactor.
Reaktoren dieser Art sind seit langem bekannt und z. B. im US-Patent 5 094 669, EP-Patent 0 078 100 und GB-Patent 2 003 5S9 beschrieben. Die Vergasung erfolgt mit Hilfe eines Drehrosts im Reaktor und dem Abzug fester Asche oder ohne Drehrost mit Abzug flüssiger Schlacke. Als Brennstoff verwendet man Kohle aller Art, auch Braunkohle und Torf, dazu können verschiedenartige Abfallstoffe zugegeben werden. Wenn der von oben auf das Festbett gegebene Brennstoff zu feinkörnig ist, wird ein störend großer Anteil davon durch das Produktgas aus dem Reaktor abgezogen und in die anschließenden Apparate transportiert. Dies kann zu Betriebsstörungen führen, die den Stillstand des Reaktors nötig machen. Auch durch Steigerung der Maximalleistung eines Reaktors und damit erhöhter Produktgaserzeugung kann es geschehen, daß der Produktgasstrom zuviel feinkörnigen Brennstoff aus dem Reaktor transportiert.Reactors of this type have long been known and z. For example, see U.S. Patent 5,094,669, EP Patent 0,078,100 and GB Patent 2,003,5S9. Gasification takes place with the help of a rotating grate in the reactor and the removal of solid ash or without rotating grate with the removal of liquid slag. All types of coal are used as fuel, including lignite and peat, and various types of waste can be added. If the fuel placed on top of the fixed bed is too fine-grained, a disruptive large proportion of it is drawn off from the reactor by the product gas and transported to the subsequent apparatus. This can lead to malfunctions that make the reactor standstill necessary. Also by increasing the maximum output of a reactor and thus increasing product gas generation, it can happen that the product gas stream transports too much fine-grained fuel out of the reactor.
Der Erfindung liegt die Aufgabe zugrunde, den eingangs genannten Reaktor so auszugestalten, daß auch bei einem starken Produktgasstrom keine störenden Mengen an feinkörnigem Brennstoff aus dem Reaktor abgezogen werden. Erfindungsgemäß gelingt dies dadurch, daß im Reaktor mindestens ein Fliehkraft-Abscheider zum Abscheiden von Feststoffen aus dem Produktgas angeordnet ist, der eine Eintrittsöffnung für vom Festbett kommendes staubhaltiges Produktgas, eine Austrittsleitung für Produktgas und eine in das Festbett führende Feststoffableitung aufweist, wobei die Austrittsleitung mit dem Abzugskanal des Reaktors verbunden ist.The invention is based on the object of designing the reactor mentioned at the outset in such a way that even in the case of a strong product gas stream, no disruptive amounts of fine-grained fuel are drawn off from the reactor. This is achieved according to the invention in that at least one centrifugal separator for separating solids from the product gas is arranged in the reactor, which has an inlet opening for dust-containing product gas coming from the fixed bed, an outlet line for product gas and a solid discharge line leading into the fixed bed, the outlet line with the discharge channel of the reactor is connected.
Vorteilhaf erweise werden mehrere Fliehkraf -Abscheider im Reaktor angeordnet, wobei die Austrittsleitungen der Abscheider in eine im oberen Bereich des Reaktors angeordnete Ringkammer münden, die mit dem Abzugskanal in Verbindung steht.Advantageously, several centrifugal separators are arranged in the reactor, the outlet lines of the separators in one in the upper region of the reactor arranged annular chamber open, which is connected to the discharge channel.
Eine zweckmäßige Weiterbildung der Erfindung besteht darin, daß im oberen Bereich des Reaktors eine vertikale Ringwand angeordnet ist und daß sich die Eintrittsöffnung des Abscheiders außerhalb des von der Ringwand umschlossenen Reaktorbereichs befindet. Die Ringwand sorgt dafür, daß sich die Eintrittsöffnung des Abscheiders oberhalb des Festbettes befindet.An expedient development of the invention consists in that a vertical ring wall is arranged in the upper area of the reactor and that the inlet opening of the separator is located outside the reactor area enclosed by the ring wall. The ring wall ensures that the inlet opening of the separator is above the fixed bed.
Es bietet sich an, als Fliehkraft-Abscheider den Zyklon zu verwenden, doch können auch andere Fliehkraft-Abscheider verwendet werden. Die Reaktoren arbeiten üblicherweise bei Drücken von 1 bis 80 bar.It is advisable to use the cyclone as a centrifugal separator, but other centrifugal separators can also be used. The reactors usually operate at pressures from 1 to 80 bar.
Ausgestaltungsmöglichkeiten des Reaktors werden mit Hilfe der Zeichnung erläuter . Es zeigt :Design options of the reactor are explained with the aid of the drawing. It shows :
Fig. 1 einen Vergasungsreaktor mit Drehrost imFig. 1 shows a gasification reactor with a rotating grate in
Längsschnitt in schematischer Darstellung und Fig. 2 eine zweite Reaktor-Variante in der Darstellung analog zu Fig. 2 und Fig. 3 eine weitere Reaktor-Variante. Der Reaktor der Fig. 1 weist ein Gehäuse (1) auf, das üblicherweise wassergekühlt ist. Der körnige Brennstoff kommt aus einem Vorratsbehälter (2) und fällt durch das dann geöffnete Ventil (3) auf das Festbett (4) . Im unteren Bereich des Reaktors befindet sich ein Drehrost (5), dem man durch eine Vergasungsmittelleitung (6) ein Gemisch aus Sauerstoff und Wasserdampf zuführt, welches vom Drehrost (5) aus in das Festbett (4) hinein verteilt wird. In nicht näher dargestellter Weise zieht man Asche durch die Öffnung (7) nach unten ab.Longitudinal section in a schematic representation and FIG. 2 shows a second reactor variant in the representation analogous to FIG. 2 and FIG. 3 a further reactor variant. The reactor of FIG. 1 has a housing (1) which is usually water-cooled. The granular fuel comes from a storage container (2) and falls through the then opened valve (3) onto the fixed bed (4). In the lower area of the reactor there is a rotating grate (5), which is mixed with a gasification medium line (6) Feeds oxygen and water vapor, which is distributed from the rotating grate (5) into the fixed bed (4). In a manner not shown, ash is drawn down through the opening (7).
Die bei den endothermen Vergasungsreaktionen benötigte Energie wird durch partielle Oxidation aufgebracht. Das rohe Produktgas verläßt den Reaktor durch den Abzugskanal (9) und wird einer Kühlung und Reinigung zugeführt. Eine vertikale Ringwand (10) ist am oberen Ende gasdicht mit dem Reaktorgehäuse (1) verbunden und dient als Begrenzung für eine Ringkammer (11) , die mit dem Abzugskanal (9) in Verbindung steht. Eine horizontale Trennwand (12) ist in Form einer Ringscheibe zwischen dem Gehäuse (1) und der Ringwand (10) als untere Begrenzung der Ringkammer (11) angeordnet .The energy required in the endothermic gasification reactions is applied by partial oxidation. The crude product gas leaves the reactor through the exhaust duct (9) and is fed to cooling and cleaning. A vertical ring wall (10) is connected to the reactor housing (1) in a gas-tight manner at the upper end and serves as a boundary for an annular chamber (11) which is connected to the discharge channel (9). A horizontal partition (12) is arranged in the form of an annular disc between the housing (1) and the annular wall (10) as the lower boundary of the annular chamber (11).
In Fig. 1 sind zwei Zyklone (13) dargestellt, deren Austrittsleitungen (14) nach oben in die Ringkammer (11) führen. Die Eintrittsöffnung (15) eines jeden Zyklons (13) befindet sich unterhalb der Trennwand (12) und oberhalb des Festbettes (4) . Staubhaltiges Produktgas, das aus dem Festbett (4) herausströmt, tritt zwangsweise durch die Öffnungen (15) in einen der beiden Zyklone (13) ein, wobei die abgeschiedenen Feststoffe durch die jeweilige Feststo fableitung (16) zurück in das Festbett (4) geführt werden. Zum besseren Abfluß der Feststoffe nach unten ist der untere Bereich der Ableitung (16) aufgeweitet. Die Zahl der Zyklone kann beliebig gewählt werden, sie wird üblicherweise 1 bis 10 betragen. Das Produktgas, das die Zyklone (13) verläßt, strömt durch die Austrittsleitungen (14) zunächst in die Ringkammer (11) und dann zum Abzugskanal (9) . Der Staubgehalt dieses Produktgases ist auf diese Weise begrenzt, so daß Betriebsstörungen vermieden werden.In Fig. 1 two cyclones (13) are shown, the outlet lines (14) lead upwards into the annular chamber (11). The inlet opening (15) of each cyclone (13) is located below the partition (12) and above the fixed bed (4). Dust-containing product gas, which flows out of the fixed bed (4), forcibly enters through the openings (15) into one of the two cyclones (13), with the separated solids being discharged through the respective solid matter discharge line (16) back into the fixed bed (4) become. The lower area of the discharge line (16) is widened for better drainage of the solids downwards. The number of cyclones can be chosen arbitrarily, it will usually be 1 to 10. The product gas, which leaves the cyclones (13), flows through the outlet lines (14) first into the annular chamber (11) and then to the exhaust duct (9). The dust content of this product gas is limited in this way, so that malfunctions are avoided.
Gemäß Fig.2 befinden sich die Zyklone (13) innerhalb des von der Ringwand (10) umschlossenen Bereichs und damit mehr oder weniger im Festbett (4) , dort wo die Temperaturen relativ niedrig sind. In der Anordnung gemäß Fig. 1 befinden sich die Zyklone (13) außerhalb der Ringwand (10) und werden vom Produktgas umströmt. Die Bezugszeichen der Fig. 2 haben die bereits zusammen mit Fig. 1 erläuterte Bedeutung.According to Figure 2, the cyclones (13) are within the area enclosed by the ring wall (10) and thus more or less in the fixed bed (4), where the temperatures are relatively low. In the arrangement according to FIG. 1, the cyclones (13) are located outside the ring wall (10) and the product gas flows around them. The reference numerals of FIG. 2 have the meaning already explained together with FIG. 1.
Der schematisch dargestellte Reaktor der Fig. 3 weist nur einen Zyklon (13) auf, dessen Austrittsleitung (14) mit dem Abzugskanal (9) direkt verbunden ist. Staubhaltiges Produktgas, das vom Festbett (4) kommt, tritt durch die Öffnung (15) in den Zyklon ein, und abgeschiedene Feststoffe werden durch die Ableitung (16) zurück in das Festbett (4) geführt. Die Düsen (20) dienen der Zufuhr des Vergasungsmittels, und flüssige Schlacke wird durch den Auslaß (7a) abgezogen.3 has only one cyclone (13), the outlet line (14) of which is directly connected to the exhaust duct (9). Product gas containing dust, which comes from the fixed bed (4), enters the cyclone through the opening (15), and separated solids are returned to the fixed bed (4) through the discharge line (16). The nozzles (20) serve to supply the gasification agent and liquid slag is drawn off through the outlet (7a).
Ein Vergasungsreaktor mit Drehrost (5) , wie er in Fig. 1 oder 2 dargestellt ist, kann ohne weiteres auch nur mit einem Zyklon (13) gemäß Fig. 3 ausgerüstet sein, und ebenso kann der Reaktor der Fig. 3, der mit Abzug flüssiger Schlacke arbeitet, mehrere Abscheidezyklone (13) aufweisen, wie es zusammen mit Fig. 1 oder Fig. 2 erläutert wurde. A gasification reactor with a rotating grate (5), as shown in Fig. 1 or 2, can easily be equipped with only a cyclone (13) according to Fig. 3, and also the reactor of Fig. 3, the trigger more fluid Slag works, have several separating cyclones (13), as was explained together with FIG. 1 or FIG. 2.

Claims

Patentansprüche claims
1. Reaktor zum Vergasen körniger Brennstoffe, wobei der Brennstoff im Reaktor ein Festbett bildet, in dessen unteren Bereich sauerstoffhaltiges Vergasungsmittel eingeleitet wird, das sich im Festbett aufwärts bewegt, und wobei man Wasserstoff und Kohlenoxide enthaltendes Produktgas über dem Festbett durch einen Abzugskanal aus dem Rektor abführt, dadurch gekennzeichnet, daß im Reaktor mindestens ein Fliehkraft -Abscheider zum Abscheiden von Feststoffen aus dem Produktgas angeordnet ist, der eine Eintrittsöffnung für vom Festbett kommendes staubhaltiges Produktgas, eine Austrittsleitung für Produktgas und eine in das Festbett führende Feststoffableitung aufweist, wobei die Austrittsleitung mit dem Abzugskanal des Reaktors verbunden ist .1. Reactor for gasifying granular fuels, the fuel forming a fixed bed in the reactor, into the lower region of which oxygen-containing gasifying agent is introduced, which moves upwards in the fixed bed, and wherein product gas containing hydrogen and carbon oxides is passed over the fixed bed through an exhaust duct from the rector dissipates, characterized in that at least one centrifugal separator for separating solids from the product gas is arranged, which has an inlet opening for dust-containing product gas coming from the fixed bed, an outlet line for product gas and a solid line leading into the fixed bed, the outlet line with the discharge channel of the reactor is connected.
2. Reaktor nach Anspruch 1, dadurch gekennzeichnet, daß mehrere Fliehkraft-Abscheider im Reaktor angeordnet sind und die Austrittsleitungen der Abscheider in eine im oberen Bereich des Reaktors angeordnete Ringkammer münden, die mit dem Abzugskanal in Verbindung steht .2. Reactor according to claim 1, characterized in that a plurality of centrifugal separators are arranged in the reactor and the outlet lines of the separators open into an annular chamber arranged in the upper region of the reactor, which is connected to the discharge channel.
3. Reaktor nach Anspruch 1 oder 2, dadurch gekennzeichnet, daß im oberen Bereich des Reaktors eine vertikale Ringwand angeordnet ist und daß sich die Eintrittsöffnung des Abscheiders außerhalb des von der Ringwand umschlossenen Reaktorbereichs befindet. 3. Reactor according to claim 1 or 2, characterized in that a vertical ring wall is arranged in the upper region of the reactor and that the inlet opening of the separator is located outside the reactor region enclosed by the ring wall.
4. Reaktor nach Anspruch 3, dadurch gekennzeichnet, daß sich der Abscheider außerhalb des von der Ringwand umschlossenen Bereichs befindet.4. Reactor according to claim 3, characterized in that the separator is outside the area enclosed by the ring wall.
5. Reaktor nach Anspruch 3, dadurch gekennzeichnet, daß sich der Abscheider innerhalb des von der Ringwand umschlossenen Bereichs befindet.5. Reactor according to claim 3, characterized in that the separator is located within the area enclosed by the ring wall.
6. Reaktor nach Anspruch 1 oder einem der folgenden, dadurch gekennzeichnet, daß der Fliehkraft-Abscheider als Zyklon ausgebildet ist. 6. Reactor according to claim 1 or one of the following, characterized in that the centrifugal separator is designed as a cyclone.
EP99947283A 1998-09-11 1999-09-07 Reactor for gasifying granular fuels that form a fixed bed Expired - Lifetime EP1133539B1 (en)

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
DE19841586A DE19841586A1 (en) 1998-09-11 1998-09-11 Stationary bed fuel gasification reactor, for gasification of coal, comprises centrifugal separator for solids removal from the product gas
DE19841586 1998-09-11
PCT/EP1999/006584 WO2000015738A1 (en) 1998-09-11 1999-09-07 Reactor for gasifying granular fuels that form a fixed bed

Publications (2)

Publication Number Publication Date
EP1133539A1 true EP1133539A1 (en) 2001-09-19
EP1133539B1 EP1133539B1 (en) 2003-01-29

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Family Applications (1)

Application Number Title Priority Date Filing Date
EP99947283A Expired - Lifetime EP1133539B1 (en) 1998-09-11 1999-09-07 Reactor for gasifying granular fuels that form a fixed bed

Country Status (7)

Country Link
US (1) US7258841B1 (en)
EP (1) EP1133539B1 (en)
CN (1) CN1128201C (en)
DE (2) DE19841586A1 (en)
ES (1) ES2190251T3 (en)
WO (1) WO2000015738A1 (en)
ZA (1) ZA995847B (en)

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ES2190251T3 (en) 2003-07-16
US7258841B1 (en) 2007-08-21
EP1133539B1 (en) 2003-01-29
CN1290291A (en) 2001-04-04
DE19841586A1 (en) 2000-03-16
ZA995847B (en) 2001-03-12
CN1128201C (en) 2003-11-19
WO2000015738A1 (en) 2000-03-23
DE59904195D1 (en) 2003-03-06

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