EP0721491B1 - Device for conveying refuse into a pyrolysis reactor - Google Patents
Device for conveying refuse into a pyrolysis reactor Download PDFInfo
- Publication number
- EP0721491B1 EP0721491B1 EP94926780A EP94926780A EP0721491B1 EP 0721491 B1 EP0721491 B1 EP 0721491B1 EP 94926780 A EP94926780 A EP 94926780A EP 94926780 A EP94926780 A EP 94926780A EP 0721491 B1 EP0721491 B1 EP 0721491B1
- Authority
- EP
- European Patent Office
- Prior art keywords
- pyrolysis reactor
- waste
- transport channel
- inlet tube
- transport device
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Lifetime
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Classifications
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10B—DESTRUCTIVE DISTILLATION OF CARBONACEOUS MATERIALS FOR PRODUCTION OF GAS, COKE, TAR, OR SIMILAR MATERIALS
- C10B51/00—Destructive distillation of solid carbonaceous materials by combined direct and indirect heating
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10B—DESTRUCTIVE DISTILLATION OF CARBONACEOUS MATERIALS FOR PRODUCTION OF GAS, COKE, TAR, OR SIMILAR MATERIALS
- C10B1/00—Retorts
- C10B1/10—Rotary retorts
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10B—DESTRUCTIVE DISTILLATION OF CARBONACEOUS MATERIALS FOR PRODUCTION OF GAS, COKE, TAR, OR SIMILAR MATERIALS
- C10B53/00—Destructive distillation, specially adapted for particular solid raw materials or solid raw materials in special form
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G2203/00—Furnace arrangements
- F23G2203/20—Rotary drum furnace
- F23G2203/212—Sealing arrangements between rotary and stationary parts
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G2205/00—Waste feed arrangements
- F23G2205/12—Waste feed arrangements using conveyors
- F23G2205/121—Screw conveyor
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G2205/00—Waste feed arrangements
- F23G2205/14—Waste feed arrangements using hopper or bin
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G2900/00—Special features of, or arrangements for incinerators
- F23G2900/52001—Rotary drums with co-current flows of waste and gas
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23L—SUPPLYING AIR OR NON-COMBUSTIBLE LIQUIDS OR GASES TO COMBUSTION APPARATUS IN GENERALĀ ; VALVES OR DAMPERS SPECIALLY ADAPTED FOR CONTROLLING AIR SUPPLY OR DRAUGHT IN COMBUSTION APPARATUS; INDUCING DRAUGHT IN COMBUSTION APPARATUS; TOPS FOR CHIMNEYS OR VENTILATING SHAFTS; TERMINALS FOR FLUES
- F23L2900/00—Special arrangements for supplying or treating air or oxidant for combustion; Injecting inert gas, water or steam into the combustion chamber
- F23L2900/07002—Injecting inert gas, other than steam or evaporated water, into the combustion chambers
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23L—SUPPLYING AIR OR NON-COMBUSTIBLE LIQUIDS OR GASES TO COMBUSTION APPARATUS IN GENERALĀ ; VALVES OR DAMPERS SPECIALLY ADAPTED FOR CONTROLLING AIR SUPPLY OR DRAUGHT IN COMBUSTION APPARATUS; INDUCING DRAUGHT IN COMBUSTION APPARATUS; TOPS FOR CHIMNEYS OR VENTILATING SHAFTS; TERMINALS FOR FLUES
- F23L2900/00—Special arrangements for supplying or treating air or oxidant for combustion; Injecting inert gas, water or steam into the combustion chamber
- F23L2900/07008—Injection of water into the combustion chamber
Definitions
- the invention relates to a transport device for Waste, in which a waste feed shaft is connected to a transport channel is connected, in the longitudinal direction one of one Motor drivable stuffing screw is arranged, and at the the transport channel into a pyrolysis reactor, in particular in a smoldering drum rotatable about its longitudinal axis.
- the transport device becomes thermal waste disposal used, especially after the smoldering-burning process.
- the procedure and a plant for thermal waste disposal operating afterwards are for example in EP-A-0 302 310 and in DE-A-38 30 153 and also described in EP-A-0 360 052.
- the plant for thermal waste disposal after the smoldering process contains as essential components a pyrolysis reactor and a high-temperature combustion chamber.
- the pyrolysis reactor puts the over a waste transport device of the type mentioned discarded waste in a substoichiometric process Smoldering process in carbonization gas and pyrolysis residues.
- the Smoldering gas and the pyrolysis residue are then made more suitable Refurbishing the burner of the high temperature combustion chamber fed.
- Flue gas line fed to a chimney as an outlet.
- Flue gas pipes are in particular a heat recovery steam generator as a cooling device, a dust filter system and a flue gas cleaning system built-in.
- a gas compressor which is located directly at the exit of the Flue gas cleaning system arranged and as a suction fan can be trained.
- the built-in gas compressor is used for Maintenance of a vacuum, even if only slight in the pyrolysis drum. Because of this negative pressure prevents carbonization gas through the ring seals of the pyrolysis drum leaks out into the environment.
- the transport device makes waste different kind, for example shredded household waste, more like household waste Industrial waste and crushed bulky waste, but also dewatered Mud fed to the smoldering drum.
- Waste transport equipment blocked or disrupted may be too large waste particles from the waste feed chute fall into the helix of the transport or stuffing screw. Avoiding a blockage of the stuffing screw is for continuous operation is required, as it is usually continuous new garbage or waste delivered. For one smooth transportation of waste it is also necessary that it does not adhere to the screw conveyor and engages with the helix turns. To achieve that, it is at Transport screws usual that strips in the housing on the wall are arranged in the space between the screw conveyor and protrude housing. If the screw conveyor rotates, the goods to be transported are passed through the bars of the screw conveyor prevented from turning. However, such strips are subject to high wear.
- DE-A-38 30 151, DE-A-38 30 152 and the DE-A-38 30 153 are pyrolysis reactors with a heating device for Known waste where supply lines for direct End heating of the waste in the smoldering drum Air outlet nozzles are provided. These supply lines are by a heating gas housing on the smoldering drum guided.
- the known constructions require special and therefore complex sealing measures.
- the object of the invention is to provide a transport device for Form waste of the type mentioned in such a way that at least a supply line leading from the outside into the pyrolysis reactor should lead, with comparatively little effort can be relocated.
- the object is achieved by the technical features of claim 1.
- In particular is in the room between the housing of the transport channel and the pyrolysis reactor at least one leading from the outside into the pyrolysis reactor Supply line arranged.
- Blockage of the stuffing screw should be avoided if possible become.
- the housing has a circular cross section, for example.
- the housing has a polygonal shape Cross-section.
- This polygonal cross section can be a trough-shaped cross section with a lower polygonal Part and an upper rectangular part. He can also be a polygon with sides of equal length.
- the supply line or lines can be all possible Serve purposes, for example the air supply in the Pyrolysis reactor.
- FIG. 1 is a transport device 2 for waste A. provided at a drop chute or waste feed chute 4 via releasable fastening means 6 to a fixed one Transport channel 8 is connected.
- the transport channel 8 is here designed as a stuffing screw trough.
- Has housing 8a a preferably polygonal cross-section, as can be seen from Figure 2.
- the longitudinal axis of the housing 8a is designated by 9.
- the transport channel 8 opens into a pyrolysis reactor 10, in in the present case in a rotating around its longitudinal axis 11 Smoldering drum with a larger number of heating pipes 12 is equipped parallel to the longitudinal axis 11.
- the heating pipes 12, of which only two in FIG. 1 and forty-eight in FIG are shown, are charged with heating gas h to Example with hot air. You are in a 12s front ring moored, to which an input pipe 13 connects concentrically.
- the end of the transport channel 8 is concentric in this input tube 13. As will be explained below, a good seal is
- the Longitudinal axis 15 extends in the longitudinal direction.
- the Shaft 16 of the plug screw 14 is via a gear 18 from driven by a motor 20.
- the waste feed chute 4 is laterally from or vertically above the transport channel 8 on the latter Arranged at the end.
- the filling opening for the waste is included 22 and the discharge opening designated 24.
- the transported Waste A closes the housing 8a there gas-tight. It can then neither air from the fill opening 22 to the discharge opening 24, still flow carbonization gas in the reverse direction.
- the screw conveyor 14 In Direction of transport behind the compression zone, which is in the Area of the section 14a of the screw conveyor 14, the screw conveyor 14 has a larger slope again. Which over the entire cross section of the transport channel 8 itself this extends the package of waste A again.
- a mechanical seal 40 is arranged at the end of the inlet pipe 13 .
- she consists of a rotating sliding ring 42 and a stationary Counter ring 44, both of which can be made of steel. Of the Counter ring 44 is fixed on a ring 46, which with the help a weld seam 48 is welded to the housing 8a.
- the Transport device 2 are operated fully filled.
- the screw conveyor 14 can not block, can within the housing 8a different due to the geometric shape located and configured alternative spaces 34 for such relative large parts can be provided.
- the Transport channel 8 can not only the polygonal shown Cross section, but also have other cross sections.
- the relatively large, parts to be transported are pressed into this alternative space 34 and with the longitudinally moving waste A in the Evacuation spaces 34 transported, so that they are the screw conveyor 14 can not block.
- the escape rooms 34 are located usually above or to the side of the screw conveyor 14.
- the waste A in the rotating smoldering drum 10 by means of the heating pipes 12 indirectly from the heating gas h heated.
- This heating gas h is via a stationary heating gas inlet housing (not shown) passed into the smoldering drum 10.
- a stationary heating gas inlet housing (not shown) passed into the smoldering drum 10.
- Heating tubes 12 attached with one end.
- the other end is in the tube sheet wall 12s moored that part of the wall a "cold" heating gas outlet housing 50 forms.
- This Housing 50 passes the heating gas h into an outlet.
- ring seals 52 or 54 are provided for sealing of the hot gas outlet housing 50 against the rotating Tube 10 and the input tube 13 ring seals 52 or 54 provided. Accordingly, to seal the Heating gas inlet housing (not shown) ring seals intended.
- the latter can be done according to the smoldering-burning method by means of a suitable device (not shown) in different combustible and inert fractions divided and sorted out be before the combustible portion of a combustion in a high temperature combustion chamber (not shown) becomes.
- At least one supply line 32 in the space 30 between the housing 8a of the transport channel 8 and the pyrolysis reactor 10 (or its inlet tube 13) also one Disposal line can be arranged.
- This disposal line can be used, for example, as a suction pipe for discharge of water vapor from the interior of the pyrolysis reactor 10 serve.
- the arrangement of a supply and / or disposal line 32 instead of at the entrance can also be provided at the outlet of the pyrolysis reactor 10, using an output pipe that joins the input pipe 13 corresponds.
Abstract
Description
Die Erfindung bezieht sich auf eine Transporteinrichtung fĆ¼r Abfall, bei der ein Abfall-ZufĆ¼hrschacht an einen Transportkanal angeschlossen ist, in dessen LƤngsrichtung eine von einem Motor antreibbare Stopfschnecke angeordnet ist, und bei der der Transportkanal in einen Pyrolysereaktor, insbesondere in eine um ihre LƤngsachse drehbare Schweltrommel, mĆ¼ndet. Die Transporteinrichtung wird zur thermischen Abfallentsorgung eingesetzt, insbesondere nach dem Schwel-Brenn-Verfahren.The invention relates to a transport device for Waste, in which a waste feed shaft is connected to a transport channel is connected, in the longitudinal direction one of one Motor drivable stuffing screw is arranged, and at the the transport channel into a pyrolysis reactor, in particular in a smoldering drum rotatable about its longitudinal axis. The transport device becomes thermal waste disposal used, especially after the smoldering-burning process.
Auf dem Gebiet der Abfallbeseitigung ist das sogenannte Schwel-Brenn-Verfahren bekannt geworden. Das Verfahren und eine danach arbeitende Anlage zur thermischen Abfallentsorgung sind beispielsweise in der EP-A-0 302 310 sowie in der DE-A-38 30 153 und auch in der EP-A-0 360 052 beschrieben. Die Anlage zur thermischen Abfallentsorgung nach dem Schwel-Brenn-Verfahren enthƤlt als wesentliche Komponenten einen Pyrolysereaktor und eine Hochtemperatur-Brennkammer. Der Pyrolysereaktor setzt den Ć¼ber eine Abfall-Transporteinrichtung der eingangs genannten Art aufgegebenen Abfall in einem unterstƶchiometrisch ablaufenden Schwelvorgang in Schwelgas und Pyrolysereststoff um. Das Schwelgas und der Pyrolysereststoff werden sodann nach geeigneter Aufarbeitung dem Brenner der Hochtemperatur-Brennkammer zugefĆ¼hrt. Hier entsteht schmelzflĆ¼ssige Schlacke, die Ć¼ber einen Abzug entnehmbar ist und die nach AbkĆ¼hlung in verglaster Form vorliegt. Das entstehende Rauchgas wird Ć¼ber eine Rauchgasleitung einem Kamin als AuslaĆ zugefĆ¼hrt. In diese Rauchgasleitung sind insbesondere ein Abhitzedampferzeuger als KĆ¼hleinrichtung, eine Staubfilteranlage und eine Rauchgasreinigungsanlage eingebaut. Weiterhin befindet sich in der Rauchgasleitung ein Gasverdichter, der direkt am Ausgang der Rauchgasreinigungsanlage angeordnet und als SaugzuggeblƤse ausgebildet sein kann. Der eingebaute Gasverdichter dient zur Aufrechterhaltung eines - wenn auch nur geringen - Unterdrucks in der Pyrolysetrommel. Durch diesen Unterdruck wird verhindert, daĆ Schwelgas durch die Ringdichtungen der Pyrolysetrommel nach auĆen in die Umgebung austritt.In the field of waste disposal is the so-called Smoldering process became known. The procedure and a plant for thermal waste disposal operating afterwards are for example in EP-A-0 302 310 and in DE-A-38 30 153 and also described in EP-A-0 360 052. The plant for thermal waste disposal after the smoldering process contains as essential components a pyrolysis reactor and a high-temperature combustion chamber. The pyrolysis reactor puts the over a waste transport device of the type mentioned discarded waste in a substoichiometric process Smoldering process in carbonization gas and pyrolysis residues. The Smoldering gas and the pyrolysis residue are then made more suitable Refurbishing the burner of the high temperature combustion chamber fed. This creates molten slag that over a deduction is removable and the glazed after cooling Form is present. The resulting flue gas is fed through a Flue gas line fed to a chimney as an outlet. In these Flue gas pipes are in particular a heat recovery steam generator as a cooling device, a dust filter system and a flue gas cleaning system built-in. Furthermore is in the Flue gas pipe a gas compressor, which is located directly at the exit of the Flue gas cleaning system arranged and as a suction fan can be trained. The built-in gas compressor is used for Maintenance of a vacuum, even if only slight in the pyrolysis drum. Because of this negative pressure prevents carbonization gas through the ring seals of the pyrolysis drum leaks out into the environment.
Durch die Transporteinrichtung wird Abfall unterschiedlicher Art, zum Beispiel zerkleinerter HausmĆ¼ll, hausmĆ¼llƤhnlicher Industrieabfall und zerkleinerter SperrmĆ¼ll, aber auch entwƤsserter Schlamm, der Schweltrommel zugeleitet.The transport device makes waste different Kind, for example shredded household waste, more like household waste Industrial waste and crushed bulky waste, but also dewatered Mud fed to the smoldering drum.
Es hat sich gezeigt, daĆ bei einer Schwel-Brenn-Anlage die Transporteinrichtung fĆ¼r Abfall blockiert oder gestƶrt werden kann, wenn vom Abfall-ZufĆ¼hrschacht zu groĆe Abfallpartikel in die Wendel der Transport- oder Stopfschnecke hineinfallen. Die Vermeidung einer Blockade der Stopfschnecke ist aber fĆ¼r einen Dauerbetrieb erforderlich, wird doch in der Regel kontinuierlich neuer MĆ¼ll oder Abfall angeliefert. FĆ¼r einen reibungslosen Transport des Abfalls ist es auch erforderlich, daĆ dieser nicht an der Transportschnecke haftet und sich mit der Schneckenwendel mitdreht. Um das zu erreichen, ist es bei Transportschnecken Ć¼blich, daĆ im GehƤuse an dessen Wand Leisten angeordnet sind, die in den Zwischenraum zwischen Transportschnecke und GehƤuse hineinragen. Wenn sich die Transportschnecke dreht, wird das zu transportierende Gut durch die Leisten der Transportschnecke am Mitdrehen gehindert. Solche Leisten unterliegen aber einem hohen VerschleiĆ.It has been shown that in a smoldering plant Waste transport equipment blocked or disrupted may be too large waste particles from the waste feed chute fall into the helix of the transport or stuffing screw. Avoiding a blockage of the stuffing screw is for continuous operation is required, as it is usually continuous new garbage or waste delivered. For one smooth transportation of waste it is also necessary that it does not adhere to the screw conveyor and engages with the helix turns. To achieve that, it is at Transport screws usual that strips in the housing on the wall are arranged in the space between the screw conveyor and protrude housing. If the screw conveyor rotates, the goods to be transported are passed through the bars of the screw conveyor prevented from turning. However, such strips are subject to high wear.
Aus der DE-A-38 30 151, der DE-A-38 30 152 und der DE-A- 38 30 153 sind Pyrolysereaktorn mit Heizeinrichtung fĆ¼r Abfall bekannt, bei denen Versorgungsleitungen fĆ¼r die direkte Beheizung des Abfalls in der Schweltrommel endseitig mit AustrittsdĆ¼sen fĆ¼r Luft versehen sind. Diese Versorgungsleitungen sind durch ein Heizgas-GehƤuse an der Schweltrommel gefĆ¼hrt. Die bekannten Konstruktionen erfordern besondere und daher aufwendige AbdichtmaĆnahmen. From DE-A-38 30 151, DE-A-38 30 152 and the DE-A-38 30 153 are pyrolysis reactors with a heating device for Known waste where supply lines for direct End heating of the waste in the smoldering drum Air outlet nozzles are provided. These supply lines are by a heating gas housing on the smoldering drum guided. The known constructions require special and therefore complex sealing measures.
Aufgabe der Erfindung ist es, eine Transporteinrichtung fĆ¼r Abfall der eingangs genannten Art derart auszubilden, daĆ zumindest eine Versorgungsleitung, die von auĆen in den Pyrolysereaktor fĆ¼hren soll, mit vergleichsweise geringem Aufwand verlegt werden kann.The object of the invention is to provide a transport device for Form waste of the type mentioned in such a way that at least a supply line leading from the outside into the pyrolysis reactor should lead, with comparatively little effort can be relocated.
Die Aufgabe wird durch die technischen Merkmale des Anspruchs 1 gelƶst.
Insbesondere ist im Raum
zwischen dem GehƤuse des Transportkanals und dem Pyrolysereaktor
mindestens eine von auĆen in den Pyrolysereaktor fĆ¼hrende
Versorgungsleitung angeordnet.The object is achieved by the technical features of
Andere AusfĆ¼hrungsformen sind in den UnteransprĆ¼chen beschrieben.Other embodiments are described in the subclaims.
Eine Blockade der Stopfschnecke sollte nach Mƶglichkeit vermieden werden. Um ein Mitdrehen des Abfalls mit der Transportschnecke zu verhindern, kann vorgesehen sein, daĆ zwischen der Transportschnecke und dem GehƤuse ein Ausweichraum vorhanden ist. Dieser ist dadurch gebildet, daĆ von der LƤngsachse der Transportschnecke senkrecht zur LƤngsachse nach auĆen gemessen zwischen dem grƶĆten Radius der Transportschnecke und der GehƤusewand in AbhƤngigkeit von der radialen Richtung, in der gemessen wird, ein unterschiedlich groĆer Abstand frei bleibt. Damit ist sichergestellt, daĆ sich der transportierte Abfall von Zeit zu Zeit von der Transportschnecke lƶsen kann, so daĆ er nicht mit der Transportschnecke rotiert.Blockage of the stuffing screw should be avoided if possible become. To turn the waste with the screw conveyor to prevent it can be provided that between the transport screw and the housing an escape room is available. This is formed by the fact that Longitudinal axis of the screw conveyor perpendicular to the longitudinal axis measured outwards between the largest radius of the screw conveyor and the housing wall depending on the radial Direction in which measurements are taken is different large distance remains free. This ensures that the transported waste from time to time Screw can loosen so that it is not with the screw rotates.
Vorteilhafterweise brauchen an der Innenwand des GehƤuses keine Leisten angebracht zu werden, was bisher Ć¼blich war, um das Gut daran zu hindern, sich mit der Transportschnecke zu drehen. WƤhrend solche Leisten einem hohen VerschleiĆ unterliegen, kann die vorliegende Transporteinrichtung weitgehend verschleiĆarm arbeiten.Advantageously need on the inner wall of the housing no ledges to be attached, which has been common to date to prevent the good from closing with the screw rotate. While such strips are subject to high wear, can the present transport device largely work with low wear.
Das GehƤuse hat beispielsweise einen kreisfƶrmigen Querschnitt.The housing has a circular cross section, for example.
Nach einem bevorzugten Beispiel hat das GehƤuse einen polygonfƶrmigen Querschnitt. Dieser polygonfƶrmige Querschnitt kann ein trogfƶrmiger Querschnitt mit einem unteren polygonfƶrmigen Teil und einem oberen rechteckigen Teil sein. Er kann auch ein Vieleck mit gleichlangen Seiten sein.According to a preferred example, the housing has a polygonal shape Cross-section. This polygonal cross section can be a trough-shaped cross section with a lower polygonal Part and an upper rectangular part. He can also be a polygon with sides of equal length.
Auch diese AusfĆ¼hrungsformen bewirken, daĆ der zu transportierende Abfall nicht mit der Transportschnecke rotiert.These embodiments also cause the one to be transported Waste does not rotate with the screw conveyor.
Die Versorgungsleitung oder -leitungen kann/kƶnnen allen mƶglichen Zwecken dienen, beispielsweise der Luftzufuhr in den Pyrolysereaktor.The supply line or lines can be all possible Serve purposes, for example the air supply in the Pyrolysis reactor.
Es lƤĆt sich die Transporteinrichtung am Eingang und/oder am
Ausgang des Pyrolysereaktors einsetzen. Generell gesprochen
handelt es sich somit um eine Transporteinrichtung fĆ¼r den
Eintrag oder Austrag von Abfall in bzw. aus einem um seine
LƤngsachse drehbaren Pyrolysereaktor, die bevorzugt gekennzeichnet
ist durch
Weitere vorteilhafte Ausgestaltungen sind in den UnteransprĆ¼chen gekennzeichnet. Further advantageous embodiments are in the subclaims featured.
AusfĆ¼hrungsbeispiele der Erfindung werden im folgenden anhand
von zwei Figuren nƤher erlƤutert. Es zeigen:
Nach Figur 1 ist eine Transporteinrichtung 2 fĆ¼r Abfall A
vorgesehen, bei der ein Fallschacht oder Abfall-ZufĆ¼hrschacht
4 Ć¼ber lƶsbare Befestigungsmittel 6 an einen feststehenden
Transportkanal 8 angeschlossen ist. Der Transportkanal 8 ist
hier als Stopfschnecken-Trog ausgebildet. Sein GehƤuse 8a hat
einen bevorzugt polygonalen Querschnitt, wie aus Figur 2 hervorgeht.
Die LƤngsachse des GehƤuses 8a ist mit 9 bezeichnet.
Der Transportkanal 8 mĆ¼ndet in einen Pyrolysereaktor 10, im
vorliegenden Fall in eine sich um ihre LƤngsachse 11 drehende
Schweltrommel, die mit einer grƶĆeren Anzahl von Heizrohren
12 parallel zur LƤngsachse 11 ausgerĆ¼stet ist. Die Heizrohre
12, von denen in Figur 1 nur zwei und in Figur 2 achtundvierzig
dargestellt sind, werden mit Heizgas h beschickt, zum
Beispiel mit heiĆer Luft. Sie sind in einem Stirnring 12s
festgemacht, an den sich konzentrisch ein Eingangsrohr 13 anschlieĆt.
Das Ende des Transportkanals 8 liegt konzentrisch
in diesem Eingangsrohr 13. Wie weiter unten dargelegt wird,
ist dabei fĆ¼r eine gute Abdichtung gesorgt.According to Figure 1 is a
Im Inneren des im Normalbetrieb feststehenden Transportkanals
8 ist eine Transport- oder Stopfschnecke 14 angeordnet, deren
LƤngsachse 15 sich in dessen LƤngsrichtung erstreckt. Die
Welle 16 der Stopfenschnecke 14 ist Ć¼ber ein Getriebe 18 von
einem Motor 20 angetrieben. Der Abfall-ZufĆ¼hrschacht 4 ist
seitlich vom oder senkrecht Ć¼ber dem Transportkanal 8 an dessen
Ende angeordnet. Die EinfĆ¼llƶffung fĆ¼r den Abfall ist mit
22 und die Abgabeƶffnung mit 24 bezeichnet. Inside the transport channel, which is fixed during
Beim Transport von Abfall A vom Fallschacht 4 zur Schweltrommel
10 ist es erforderlich, daĆ weder Luftsauerstoff von der
EinfĆ¼llƶffnung 22 Ć¼ber die Abgabeƶffnung 24 zur Schweltrommel
10 gelangt, noch daĆ Schwelgas aus der Schweltrommel 10 im
Gegenstrom zum transportierten Abfall A durch die EinfĆ¼llƶffnung
22 in die Umgebung gelangt. Um das zu verhindern, hat
ein mittleres TeilstĆ¼ck 14a der Transportschnecke 14 eine geringere
Steigung als die Ć¼brige Transportschnecke 14 oder das
AnfangsstĆ¼ck 14b. Damit wird erreicht, daĆ der transportierte
Abfall A im Bereich dieses mittleren TeilstĆ¼cks 14a stƤrker
verdichtet wird als in den anderen Bereichen, was dazu fĆ¼hrt,
daĆ im Bereich des TeilstĆ¼cks 14a der Transportschnecke 14
praktisch der gesamte Teilraum im GehƤuse 8a des Transportkanals
8 durch den Abfall A ausgefĆ¼llt ist. Der transportierte
Abfall A selbst verschlieĆt dort das GehƤuse 8a gasdicht. Es
kann dann weder Luft von der EinfĆ¼llƶffnung 22 zur Abgabeƶffnung
24, noch Schwelgas in umgekehrter Richtung strƶmen. In
Transportrichtung hinter der Verdichtungszone, die sich im
Bereich des TeilstĆ¼cks 14a der Transportschnecke 14 befindet,
hat die Transportschnecke 14 wieder eine grƶĆere Steigung.
Die Ć¼ber den gesamten Querschnitt des Transportkanals 8 sich
erstreckende Packung des Abfalls A wird dadurch wieder aufgelƶst.When transporting waste A from the
Von Bedeutung ist nun, daĆ infolge der getroffenen geometrischen
Anordnung im Raum 30 zwischen dem GehƤuse 8a des Transportkanals
8 und dem Pyrolysereaktor 10 mindestens eine von
auĆen in den Pyrolysereaktor 10 fĆ¼hrende Versorgungsleitung
32 angeordnet ist. Vorliegend sind gemĆ¤Ć Figur 2 drei Versorgungsleitungen
32 vorhanden. Der betrachtete Raum 30 liegt
hier zwischen dem GehƤuse 8a und dem Eingangsrohr 13. Die
Versorgungsleitungen 32 liegen hier in den "freien Ecken"
auĆerhalb des GehƤuses 8a. Die Versorgungsleitungen 32 sind
zum Beispiel zum Einbringen von Luft 1, Inertgas, Wasser oder
Wasserdampf, der Ć¼berhitzt sein kann, vorgesehen. Die eingebrachte
Luft 1 kann zur Teilverbrennung von Schwelgas im Pyrolysereaktor
10 dienen. Zwei Luftaustritts- oder BrenndĆ¼sen
an der Versorgungsleitung 32 sind in Figur 1 mit 35 bezeichnet.
Durch das Einbringen von Ć¼berhitztem Dampf wird der Abfall
im Pyrolysereaktor direkt erwƤrmt und getrocknet.It is now important that as a result of the geometric
Arrangement in
Von Bedeutung ist auch eine gute Abdichtung des Pyrolysereaktors
10 nach auĆen. Zu diesem Zweck ist am Ende des Eingangsrohrs
13 eine Gleitringdichtung 40 angeordnet. Sie besteht
aus einem sich mitdrehenden Gleitring 42 und einem ortsfesten
Gegenring 44, die beide aus Stahl gefertigt sein kƶnnen. Der
Gegenring 44 ist auf einem Ring 46 festgemacht, der mit Hilfe
einer SchweiĆnaht 48 am GehƤuse 8a verschweiĆt ist.Good sealing of the pyrolysis reactor is also important
10 outwards. For this purpose is at the end of the inlet pipe
13 a
Um das GehƤuse 8a des Transportkanals 8 durch den transportierten
Abfall A gasdicht verschlieĆen zu kƶnnen, sollte die
Transporteinrichtung 2 voll gefĆ¼llt betrieben werden. Damit
relativ groĆe, harte Teile des Abfalls A die Transportschnecke
14 nicht blockieren kƶnnen, kƶnnen innerhalb des GehƤuses
8a infolge der geometrischen Formgebung verschieden
gelegene und konfigurierte Ausweichraume 34 fĆ¼r solche relativ
groĆen Teile vorgesehen sein. Mit anderen Worten: Der
Transportkanal 8 kann nicht nur den gezeigten polygonfƶrmigen
Querschnitt, sondern auch andere Querschnitte aufweisen. Bei
sich drehender Transportschnecke 14 werden die relativ groĆen,
zu transportierenden Teile in diese Ausweichraume 34 gedrĆ¼ckt
und mit dem in LƤngsrichtung bewegten Abfall A in den
AusweichrƤumen 34 mittransportiert, so daĆ sie die Transportschnecke
14 nicht blockieren kƶnnen. Die Ausweichraume 34 befinden
sich in der Regel oberhalb oder seitlich der Transportschnecke
14.Around the
Nach Figur 1 wird der Abfall A in der sich drehenden Schweltrommel
10 mittels der Heizrohre 12 indirekt vom Heizgas h
beheizt. Dieses Heizgas h wird Ć¼ber ein ortsfestes Heizgas-EintrittsgehƤuse
(nicht gezeigt) in die Schweltrommel 10 geleitet.
An deren Rohrbodenwand sind die parallel verlaufenden
Heizrohre 12 mit einem Ende befestigt. Das andere Ende ist in
der Rohrbodenwand 12s festgemacht, die einen Teil der Wand
eines "kalten" Heizgas-AustrittsgehƤuses 50 bildet. Von diesem
GehƤuse 50 gelangt das Heizgas h in einen AuslaĆ. Zur Abdichtung
des Heizgas-AustrittsgehƤuses 50 gegen das sich drehende
Rohr 10 und das Eingangsrohr 13 sind Ringdichtungen 52
bzw. 54 vorgesehen. Entsprechend sind zur Abdichtung des
Heizgas-EintrittsgehƤuses (nicht gezeigte) Ringdichtungen
vorgesehen. Vom Innenraum der Schweltrommel 10, genauer: vom
"heiĆen" Rohrboden, ist ein (nicht gezeigtes) Austragsrohr in
den Innenraum einer feststehenden Austragsvorrichtung geleitet.
Das Ć¼ber das Austragsrohr in diese Austragsvorrichtung
gelangende Schwelgut wird dort in Schwelgas und Reststoff
aufgeteilt. Letzterer kann gemĆ¤Ć dem Schwel-Brenn-Verfahren
mittels einer geeigneten Vorrichtung (nicht gezeigt) in verschiedene
brennbare und inerte Fraktionen aufgeteilt und aussortiert
werden, bevor der brennbare Anteil einer Verbrennung
in einer (nicht gezeigten) Hochtemperatur-Brennkammer zugefĆ¼hrt
wird.According to Figure 1, the waste A in the rotating smoldering
Es soll noch darauf hingewiesen werden, daĆ anstelle oder zusƤtzlich
zu mindestens einer Versorgungsleitung 32 natĆ¼rlich
im Raum 30 zwischen dem GehƤuse 8a des Transportkanals 8 und
dem Pyrolysereaktor 10 (oder dessen Eingangsrohr 13) auch eine
Entsorgungsleitung angeordnet sein kann. Diese Entsorgungsleitung
kann zum Beispiel als Absaugrohr fĆ¼r die Ableitung
von Wasserdampf aus dem Innenraum des Pyrolysereaktors
10 dienen. Auch ist anzumerken, daĆ die Anordnung einer Versorgungs-
und/oder Entsorgungsleitung 32 anstelle am Eingang
auch am Ausgang des Pyrolysereaktors 10 vorgesehen sein kann,
und zwar unter Verwendung eines Ausgangsrohrs, das dem Eingangsrohr
13 entspricht.It should be noted that instead of or in addition
to at least one
Claims (8)
- Transport device (2) for waste (A), with a waste feed chute (4) being connected to a transport channel (8), in the longitudinal direction of which transport channel a screw conveyor (14), which can be driven by a motor (20), is arranged, with the transport channel (8) opening into a pyrolysis reactor (10), in particular into a low-temperature carbonization drum which is rotatable about its longitudinal axis (11), and with at least one supply line (32), which leads from the outside into the pyrolysis reactor (10), being arranged in the area between the housing (8a) of the transport channel (8) and the pyrolysis reactor (10),
characterized in that the pyrolysis reactor (10) is firmly connected on the input side to an inlet tube (13), which has a smaller cross section than the pyrolysis reactor (10), in that the transport channel (8) is sealed on the end and is fixedly arranged within the inlet tube (13), and in that the supply line (32) is guided through the area (30) between the inlet tube (13) and the transport channel (8). - Transport device according to claim 1,
characterized in that the housing (8a) of the transport channel (8) has a non-round, in particular a polygonal, cross section. - Transport device according to claim 1 or 2,
characterized in that the inlet tube (13) is provided with a sliding seal (40) at the end. - Transport device according to claim 1, 2 or 3,
characterized in that a chamber (50) for the passage of heating gas (h) is fastened in a sliding manner on the inlet tube (13). - Transport device according to one of claims 1 to 4, characterized in that the supply line (32) is provided for the transportation of inert gas, water, water vapour, in particular air (1).
- Transport device according to one of claims 1 to 5, characterized in that the supply line (32) in the pyrolysis reactor (10) is provided with an outlet nozzle (35).
- Transport device according to one of claims 1 to 6, characterized in that the screw conveyor (14) has sections (14a, 14b) of variable rise.
- Transport device (2) according to one of claims 1 to 7, characterized by a sealing ring (42) fastened at the end to the inlet tube (13) and by a counter ring (44) for the sealing ring (42), with the counter ring being fastened to the outer circumference of the transport channel (8).
Applications Claiming Priority (3)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE4332865 | 1993-09-27 | ||
DE4332865A DE4332865A1 (en) | 1993-09-27 | 1993-09-27 | Device for transporting waste in a pyrolysis reactor |
PCT/DE1994/001058 WO1995009217A1 (en) | 1993-09-27 | 1994-09-14 | Device for conveying refuse into a pyrolysis reactor |
Publications (2)
Publication Number | Publication Date |
---|---|
EP0721491A1 EP0721491A1 (en) | 1996-07-17 |
EP0721491B1 true EP0721491B1 (en) | 1999-12-01 |
Family
ID=6498751
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP94926780A Expired - Lifetime EP0721491B1 (en) | 1993-09-27 | 1994-09-14 | Device for conveying refuse into a pyrolysis reactor |
Country Status (17)
Country | Link |
---|---|
US (1) | US5709779A (en) |
EP (1) | EP0721491B1 (en) |
JP (1) | JP3121018B2 (en) |
KR (1) | KR100304307B1 (en) |
CN (1) | CN1056872C (en) |
AT (1) | ATE187195T1 (en) |
CA (1) | CA2172634A1 (en) |
CZ (1) | CZ74896A3 (en) |
DE (2) | DE4332865A1 (en) |
DK (1) | DK0721491T3 (en) |
ES (1) | ES2140554T3 (en) |
HU (1) | HU216412B (en) |
PL (1) | PL313586A1 (en) |
PT (1) | PT721491E (en) |
RU (1) | RU2100402C1 (en) |
SK (1) | SK281845B6 (en) |
WO (1) | WO1995009217A1 (en) |
Families Citing this family (21)
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---|---|---|---|---|
DE19700653C1 (en) * | 1997-01-10 | 1998-04-02 | Siemens Ag | Grinding and feeding arrangement for refuse, especially for an incinerator |
DE19700655C1 (en) * | 1997-01-10 | 1998-04-02 | Siemens Ag | Refuse conveyor, especially for feeding a pyrolytic refuse incinerator |
WO2002055631A1 (en) * | 2001-01-15 | 2002-07-18 | Takamo Industries Co., Ltd. | Plastic liquefying device |
DE10202490C1 (en) * | 2002-01-23 | 2003-12-04 | Schwaebische Huettenwerke Gmbh | Device for introducing secondary fuels into an incineration plant |
DE102004010407B4 (en) * | 2004-03-01 | 2013-02-21 | Kbi International Ltd. | Reactor for thermal waste treatment |
DE102004016993B4 (en) * | 2004-04-02 | 2014-11-06 | Kbi International Ltd. | Thermal waste treatment reactor with a feed channel and thermal waste treatment process |
CN2878390Y (en) * | 2006-04-07 | 2007-03-14 | ēę°ę | Multi-functional full automatic remote constant temperature heat supply cracking device for waste and old tyre |
RU2392543C2 (en) | 2008-02-22 | 2010-06-20 | ŠŠ°ŠŗŃŃŃŠ¾Šµ ŠŠŗŃŠøŠ¾Š½ŠµŃŠ½Š¾Šµ ŠŠ±ŃŠµŃŃŠ²Š¾ "Š¤ŠøŠ½Š°Š½ŃŠ¾Š²Š¾-ŠŃŠ¾Š¼ŃŃŠ»ŠµŠ½Š½Š°Ń ŠŃŃŠæŠæŠ° "Š¢ŠµŠ·Š°ŃŃŃŠ¼" | Method and device for processing of domestic and industrial organic wastes |
CN102369408B (en) * | 2009-03-17 | 2014-11-05 | T.D.E.åę¶ęęÆęéå ¬åø | A pyrolytic reactor |
CN101760220A (en) * | 2010-01-12 | 2010-06-30 | čåŗåøé”ŗé«ē ¤åå·„ē§ęęéå ¬åø | Method for continuously coking coal liquefaction residuals and equipment thereof |
CN102274845B (en) * | 2010-06-12 | 2015-03-18 | äøęµ·äøē§å²øč¾¾čč½äŗ§åē§ęęéå ¬åø | Municipal refuse low-temperature oxygen-free carbonization system equipment and low-temperature oxygen-free carbonization revolving furnace therefor |
WO2012136344A1 (en) * | 2011-04-06 | 2012-10-11 | Olabil Vermƶgensverwaltungsgesellschaft Mbh | Conveying element for conveying a product, and method for carrying out a pyrolytic process using such a conveying element |
EP3053725A1 (en) * | 2015-02-06 | 2016-08-10 | LANXESS Deutschland GmbH | Plug screw |
CN105131998A (en) * | 2015-07-09 | 2015-12-09 | åäŗ¬äøēæē§č½ęęÆęéå ¬åø | Biomass and coal medium-low temperature pyrolysis quality improving system and technology thereof |
CN105505410B (en) * | 2015-11-30 | 2018-09-04 | åēµéå·„č”份ęéå ¬åø | A kind of rotary dry distillation stove charging gear and its feeding method |
US10280377B1 (en) * | 2016-03-24 | 2019-05-07 | Helge Carl Nestler | Pyrolysis and steam cracking system |
US20190085247A1 (en) * | 2016-05-06 | 2019-03-21 | Aemerge Llc | Rotating drum device for use with carbonizer system and process of use thereof |
CN106753460A (en) * | 2016-11-14 | 2017-05-31 | ę°ēē§ē«ęŗę¢°č®¾å¤ęéå ¬åø | Feeding device is dried in self sealss water squeezing |
CN107159686A (en) * | 2017-07-05 | 2017-09-15 | ęé½äøčæē§ęęéå ¬åø | A kind of vehicle-mounted movable stalk and waste plastics mulch film are while continuous processing system |
CN109609155B (en) * | 2019-01-11 | 2021-03-05 | ę¬å·å·„äøčäøęęÆå¦é¢ | Biomass carbonization feeding device |
US11561006B2 (en) * | 2020-10-23 | 2023-01-24 | M.S.T. Corporation | Apparatus and process for a kinetic feed plug screw |
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US1480152A (en) * | 1917-04-14 | 1924-01-08 | Gen Reduction Gas & By Product | Gas producer |
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US2723226A (en) * | 1953-05-04 | 1955-11-08 | Lesher And Associates Inc | Low temperature carbonization process |
US4142867A (en) * | 1974-07-04 | 1979-03-06 | Karl Kiener | Apparatus for the production of combustible gas |
US4074979A (en) * | 1975-04-28 | 1978-02-21 | Mitsubishi Jukogyo Kabushiki Kaisha | Thermal decomposition apparatus |
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US4465556A (en) * | 1981-07-16 | 1984-08-14 | American Carbons, Inc. | Pyrolysis system with hot gas recirculation |
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US4734166A (en) * | 1987-02-05 | 1988-03-29 | Angelo Ii James F | Furnace for the selective incineration or carbonization of waste materials |
DE3811820A1 (en) * | 1987-08-03 | 1989-02-16 | Siemens Ag | METHOD AND SYSTEM FOR THERMAL WASTE DISPOSAL |
EP0360052B1 (en) * | 1988-09-05 | 1992-07-29 | Siemens Aktiengesellschaft | Pyrolysis reactor for the thermal disposal of waste |
DE3830152A1 (en) * | 1988-09-05 | 1990-03-15 | Siemens Ag | Pyrolysis reactor for thermal waste disposal |
DE3830151A1 (en) * | 1988-09-05 | 1990-03-15 | Siemens Ag | Pyrolysis reactor with heating device |
DE3830153A1 (en) * | 1988-09-05 | 1990-03-15 | Siemens Ag | Pyrolysis reactor with indirect and direct heating |
-
1993
- 1993-09-27 DE DE4332865A patent/DE4332865A1/en not_active Withdrawn
-
1994
- 1994-09-14 HU HU9600748A patent/HU216412B/en not_active IP Right Cessation
- 1994-09-14 PL PL94313586A patent/PL313586A1/en unknown
- 1994-09-14 CN CN94193564A patent/CN1056872C/en not_active Expired - Fee Related
- 1994-09-14 ES ES94926780T patent/ES2140554T3/en not_active Expired - Lifetime
- 1994-09-14 AT AT94926780T patent/ATE187195T1/en not_active IP Right Cessation
- 1994-09-14 CZ CZ96748A patent/CZ74896A3/en unknown
- 1994-09-14 CA CA002172634A patent/CA2172634A1/en not_active Abandoned
- 1994-09-14 RU RU96108254/25A patent/RU2100402C1/en not_active IP Right Cessation
- 1994-09-14 JP JP07510044A patent/JP3121018B2/en not_active Expired - Fee Related
- 1994-09-14 PT PT94926780T patent/PT721491E/en unknown
- 1994-09-14 KR KR1019960701546A patent/KR100304307B1/en not_active IP Right Cessation
- 1994-09-14 WO PCT/DE1994/001058 patent/WO1995009217A1/en not_active Application Discontinuation
- 1994-09-14 SK SK367-96A patent/SK281845B6/en unknown
- 1994-09-14 DK DK94926780T patent/DK0721491T3/en active
- 1994-09-14 DE DE59408969T patent/DE59408969D1/en not_active Expired - Fee Related
- 1994-09-14 EP EP94926780A patent/EP0721491B1/en not_active Expired - Lifetime
-
1996
- 1996-03-27 US US08/625,404 patent/US5709779A/en not_active Expired - Fee Related
Also Published As
Publication number | Publication date |
---|---|
KR100304307B1 (en) | 2001-11-22 |
ES2140554T3 (en) | 2000-03-01 |
HU9600748D0 (en) | 1996-05-28 |
CN1056872C (en) | 2000-09-27 |
PT721491E (en) | 2000-05-31 |
HUT74783A (en) | 1997-02-28 |
HU216412B (en) | 1999-06-28 |
CN1131963A (en) | 1996-09-25 |
KR960704999A (en) | 1996-10-09 |
DE59408969D1 (en) | 2000-01-05 |
SK36796A3 (en) | 1997-06-04 |
PL313586A1 (en) | 1996-07-08 |
US5709779A (en) | 1998-01-20 |
JPH09501982A (en) | 1997-02-25 |
WO1995009217A1 (en) | 1995-04-06 |
CA2172634A1 (en) | 1995-04-06 |
EP0721491A1 (en) | 1996-07-17 |
JP3121018B2 (en) | 2000-12-25 |
DE4332865A1 (en) | 1995-03-30 |
CZ74896A3 (en) | 1996-07-17 |
RU2100402C1 (en) | 1997-12-27 |
DK0721491T3 (en) | 2000-05-29 |
ATE187195T1 (en) | 1999-12-15 |
SK281845B6 (en) | 2001-08-06 |
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