EP0716676B1 - Rotary heating chamber for solids - Google Patents
Rotary heating chamber for solids Download PDFInfo
- Publication number
- EP0716676B1 EP0716676B1 EP94924703A EP94924703A EP0716676B1 EP 0716676 B1 EP0716676 B1 EP 0716676B1 EP 94924703 A EP94924703 A EP 94924703A EP 94924703 A EP94924703 A EP 94924703A EP 0716676 B1 EP0716676 B1 EP 0716676B1
- Authority
- EP
- European Patent Office
- Prior art keywords
- heating
- tubes
- wall
- heating tubes
- smoldering
- 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
Links
- 238000010438 heat treatment Methods 0.000 title claims abstract description 100
- 239000007787 solid Substances 0.000 title description 9
- 239000002699 waste material Substances 0.000 claims abstract description 25
- 238000003763 carbonization Methods 0.000 claims abstract description 10
- 239000011343 solid material Substances 0.000 claims abstract 2
- 239000000463 material Substances 0.000 abstract description 6
- 239000007789 gas Substances 0.000 description 13
- 238000000197 pyrolysis Methods 0.000 description 12
- 230000002093 peripheral effect Effects 0.000 description 7
- 238000000034 method Methods 0.000 description 5
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 description 4
- 238000002485 combustion reaction Methods 0.000 description 4
- 239000003546 flue gas Substances 0.000 description 4
- 239000002184 metal Substances 0.000 description 4
- 238000001816 cooling Methods 0.000 description 2
- 239000000428 dust Substances 0.000 description 2
- 230000001788 irregular Effects 0.000 description 2
- 238000012423 maintenance Methods 0.000 description 2
- 230000008439 repair process Effects 0.000 description 2
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 1
- 229910000831 Steel Inorganic materials 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 239000000919 ceramic Substances 0.000 description 1
- 238000005352 clarification Methods 0.000 description 1
- 238000004140 cleaning Methods 0.000 description 1
- 239000000571 coke Substances 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 238000013461 design Methods 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- 230000007717 exclusion Effects 0.000 description 1
- 239000010814 metallic waste Substances 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 238000011084 recovery Methods 0.000 description 1
- 230000000284 resting effect Effects 0.000 description 1
- 238000007665 sagging Methods 0.000 description 1
- 239000002893 slag Substances 0.000 description 1
- 239000002910 solid waste Substances 0.000 description 1
- 239000010959 steel Substances 0.000 description 1
- 238000012549 training Methods 0.000 description 1
- 238000012546 transfer Methods 0.000 description 1
- 238000010626 work up procedure Methods 0.000 description 1
Images
Classifications
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- 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
-
- 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
- C10B47/00—Destructive distillation of solid carbonaceous materials with indirect heating, e.g. by external combustion
- C10B47/28—Other processes
- C10B47/30—Other processes in rotary ovens or retorts
-
- 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
- F23G2900/00—Special features of, or arrangements for incinerators
- F23G2900/50201—Waste pyrolysis, gasification or cracking by indirect heat transfer
-
- 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
Definitions
- the invention relates to a rotatable around its longitudinal axis Heating chamber for solid goods, especially on a smoldering drum for waste, with a number housed inside, approximately parallel aligned heating pipes.
- the heating chamber is used in particular as a smoldering drum for waste used for the purpose of thermal waste disposal, preferred after the smoldering process.
- the plant for thermal waste disposal using the smoldering-burning process contains a as essential components Smoldering chamber (pyrolysis reactor) and a high-temperature combustion chamber.
- the smoldering chamber uses a waste transport device abandoned waste in carbonization gases and pyrolysis residues around.
- the carbonization gases and the pyrolysis residues are then, after suitable work-up, the burner of the high-temperature combustion chamber fed.
- the high temperature combustion chamber creates molten slag that over a Deduction is removed and after cooling in glassy Form is present.
- the resulting flue gas is fed through a flue gas line fed to a chimney as an outlet.
- In this flue gas pipe are in particular a heat recovery steam generator as Cooling device, a dust filter system and a flue gas cleaning system built-in.
- a smoldering chamber (pyrolysis reactor) is usually one rotating, relatively long smoldering drum used has a large number of parallel heating pipes on the inside where the waste is largely heated in the absence of air becomes.
- the smoldering drum rotates about its longitudinal axis.
- the longitudinal axis is preferably somewhat opposite the horizontal inclined so that the solid char at the exit of the Collect the smoldering drum and from there via a discharge pipe can be carried out.
- When turning the waste through the heating pipes are lifted up and fall down again.
- the transport of the solid Dust, chunks of carbon (coke), stones, bottles, Metal, ceramic parts, etc.
- the object of the present invention is a heating chamber of the type mentioned in such a way that in the area a sufficiently large inside wall of the heating chamber Heating surface in the form of heating pipes for heating or pyrolysis of the discarded waste is available.
- the risk of metal parts jamming and other solid chunks should be greatly reduced, so that the side facing the inner wall of the heating chamber individual heating tubes optimally used for heat transfer can be.
- This object is achieved in that the Heating pipes - seen in cross section - in a practically closed one Row arranged along the wall of the interior are, and that the distance of the heating pipes (12b) from the wall of the Interior (13) and the mutual distance between the heating tubes (12b) smaller than is half the diameter of a heating tube (12b).
- the invention is therefore based on the consideration that the Ensure availability of a high heating surface lets that the individual heating pipes on the inner wall if possible be arranged closely. In other words, to prevent that the chunks mentioned get stuck in the space the heating pipes on the inside of the drum a practically closed jacket, with a cylindrical one So smolder drum form a tube circle. The distances between the individual heating pipes should be as narrow as possible to get voted.
- the main advantages are there too see that only fine waste material on the inner wall the heating chamber can fall, and that this inner wall mechanically is practically not burdened. It also follows a good one for a pyrolysis reactor or a smoldering drum Heat exchange from the heating pipes into the gas atmosphere and in the fines layer. The heat radially from the heating pipes is emitted to the outside, is therefore used very well.
- the on the inner wall of the Heating chamber located heating pipes are protected against falling coarse material from so-called impact shells from one resistant material. This is in particular around semi-cylindrical shells. Such protection can also be provided for heating pipes that are - on straight or curved lines (seen in cross section) - inside extend into the heating chamber.
- Training provided that - if necessary in the area of a such manhole blind pipes (dummies) in the series of Heating pipes are used.
- dummies manhole blind pipes
- These dummy pipes are pipes that are not flowed through by a heating gas. You are preferred arranged easily removable. This means that when the heating chamber is in operation, the row of heating pipes on the inner wall is closed while being inspected by the Personnel in the area of the manhole by dismantling the dummy pipes is interrupted.
- the blind pipes mentioned above should be the same Have diameters like the peripheral ones arranged on the inner wall Heating pipes.
- the distance of the (preferably closed) pipe circle from the The inner wall of the heating chamber should be as small as possible. He will usually be determined by design specifications, for example by attaching the heating and / or Blind pipes on end plates. Usually this distance can are between 20 and 40 mm.
- the smoldering chamber 8 is in the Embodiment an internally heated, about its longitudinal axis 10 rotating smoldering or pyrolysis drum, which is a length of 15 to 30 m, which works at 300 to 600 ° C, which is operated largely with the exclusion of oxygen and which, in addition to volatile carbonization gas, is a largely solid pyrolysis residue generated.
- Smoldering drum 8 It is an internally drilled one Smoldering drum 8 with a variety (for example 50 to 200) of heating pipes aligned parallel to each other 12, of which only four are shown in Figure 1, the interior 13 are arranged.
- On the right or “hot” end is an inlet for heating gas h in the form of a dormant, sealed Heating gas inlet chamber 14 is provided, and on the left or “Cold” end is an outlet for the heating gas h in the form of a resting, sealed heating gas outlet chamber 16 is arranged.
- the longitudinal axis 10 of the smoldering drum 8 is preferably opposite inclined horizontally so that the outlet is on the right
- the "hot" end is lower than the inlet shown on the left for waste A.
- the smoldering drum 8 is preferably on slight negative pressure kept from the environment.
- the pyrolysis drum 8 is on the output or discharge side a rotating central discharge pipe 17 a discharge device 18 downstream, with a carbonization gas discharge nozzle 20 for the discharge of the carbonization gas s and with a Pyrolysis residue outlet 22 for the discharge of the solid pyrolysis residue f is provided.
- a carbonization gas discharge nozzle 20 for the discharge of the carbonization gas s
- a Pyrolysis residue outlet 22 for the discharge of the solid pyrolysis residue f is provided.
- One at the smoldering gas discharge nozzle 20 connected carbonization line is connected to the Burner of a high temperature combustion chamber (not shown) connected.
- the rotational movement of the smoldering drum 8 about its longitudinal axis 10 is effected by a drive 24 in the form of a gear, which is connected to a motor 26.
- the bearings of the smoldering drum 8 are designated by 27.
- the heating tubes 12 each with one end at a first end plate 28 and with her other end are attached to a second end plate 30.
- the attachment to the end plates 28, 30 is made so that preferred easy replacement of the heating pipes 12 results.
- the end of the heating tubes 12 projects through an opening from the interior 13 to the left into the outlet chamber 16 or to the right into the inlet chamber 14.
- the The axis of the heating tubes 12 is perpendicular to the surface of the end plates 28, 30 aligned.
- the individual heating tubes 12th are thermally and mechanically highly stressed, and that the end plates 28, 30, which are also called tube plates or drum tube plates could be referred to the longitudinal axis 10 of the Turn smoldering drum 8 too.
- first support point X is about a third (1/3 1) and the second base Y about two thirds (2/3 1) of the total length 1 of the smoldering drum 8.
- Support or support brackets 31, 32 in the form of rounded perforated plates made of metal, for example steel. she are attached to the inner wall 33.
- the heating tubes 12 can be arranged in one configuration be as shown in Figure 2 and Figure 3. Then there are a variety of peripherally arranged heating pipes 12b and a plurality along curved or straight lines arranged heating tubes 12a for heating the more centrally lying waste. The curvature depends on the rotation the smoldering drum 8, which is indicated by an arrow 35.
- the non-radial rows start according to FIGS. 2 and 3, respectively in the area of the inner wall 33. They are - and that is from of particular importance - curved against the direction of rotation 35 (see Figure 2) or inclined (see Figure 3). Thereby it is guaranteed that when rotating about the longitudinal axis 10 waste A accumulating on the heating pipes 12a, 12b Fall down early and therefore no significant drop can reach. This eliminates the risk of damage from Chunks contained in waste A are effectively reduced.
- an obtuse angle ⁇ is shown in FIG the alignment of the individual rows to the tangent entered the wall of the smoldering drum 8.
- FIG. 3 are on a single linear row protection or Baffles 40 shown.
- the remaining linear rows as well as the curved rows of heating tubes 12a in Figure 2 - facing the central axis 10 also with such Baffles 40 made of resistant material.
- baffles 50 the peripheral ones Heating tubes 12b can be provided in Figures 2 and 3. Of these baffles 50 are for clarity only two shown in FIG.
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Materials Engineering (AREA)
- Organic Chemistry (AREA)
- Combustion & Propulsion (AREA)
- Processing Of Solid Wastes (AREA)
- Gasification And Melting Of Waste (AREA)
- Muffle Furnaces And Rotary Kilns (AREA)
- Coke Industry (AREA)
- Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
- Details Of Heat-Exchange And Heat-Transfer (AREA)
- Drying Of Solid Materials (AREA)
- Tunnel Furnaces (AREA)
- Constitution Of High-Frequency Heating (AREA)
- Feeding, Discharge, Calcimining, Fusing, And Gas-Generation Devices (AREA)
- Carbon And Carbon Compounds (AREA)
- Glass Compositions (AREA)
- Incineration Of Waste (AREA)
- Washing And Drying Of Tableware (AREA)
- Crystals, And After-Treatments Of Crystals (AREA)
- Centrifugal Separators (AREA)
Abstract
Description
Die Erfindung bezieht sich auf eine um ihre Langsachse drehbare Heizkammer für Festgut, insbesondere auf eine Schweltrommel für Abfall, mit einer Anzahl im Innenraum untergebrachter, etwa parallel zueinander ausgerichteter Heizrohre.The invention relates to a rotatable around its longitudinal axis Heating chamber for solid goods, especially on a smoldering drum for waste, with a number housed inside, approximately parallel aligned heating pipes.
Die Heizkammer wird insbesondere als Schweltrommel für Abfall zum Zwecke der thermischen Abfallentsorgung eingesetzt, bevorzugt nach dem Schwel-Brenn-Verfahren.The heating chamber is used in particular as a smoldering drum for waste used for the purpose of thermal waste disposal, preferred after the smoldering 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 beschrieben. Die Anlage zur thermischen Abfallentsorgung nach dem Schwel-Brenn-Verfahren enthält als wesentliche Komponenten eine Schwelkammer (Pyrolysereaktor) und eine Hochtemperatur-Brennkammer. Die Schwelkammer setzt den über eine Abfall-Transporteinrichtung aufgegebenen Abfall in Schwelgase und Pyrolysereststoff um. Die Schwelgase und der Pyrolysereststoff werden sodann nach geeigneter Aufarbeitung dem Brenner der Hochtemperatur-Brennkammer zugeführt. In der Hochtemperatur-Brennkammer entsteht schmelzflüssige Schlacke, die über einen Abzug entnommen wird und die nach Abkühlung in glasartiger Form vorliegt. Das entstehende Rauchgas wird über eine Rauchgasleitung einem Kamin als Auslaß zugeführt. In diese Rauchgasleitung sind insbesondere ein Abhitzedampferzeuger als Kühleinrichtung, eine Staubfilteranlage und eine Rauchgasreinigungsanlage eingebaut.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 described, for example, in EP-A-0 302 310. The plant for thermal waste disposal using the smoldering-burning process contains a as essential components Smoldering chamber (pyrolysis reactor) and a high-temperature combustion chamber. The smoldering chamber uses a waste transport device abandoned waste in carbonization gases and pyrolysis residues around. The carbonization gases and the pyrolysis residues are then, after suitable work-up, the burner of the high-temperature combustion chamber fed. In the high temperature combustion chamber creates molten slag that over a Deduction is removed and after cooling in glassy Form is present. The resulting flue gas is fed through a flue gas line fed to a chimney as an outlet. In this flue gas pipe are in particular a heat recovery steam generator as Cooling device, a dust filter system and a flue gas cleaning system built-in.
Als Schwelkammer (Pyrolysereaktor) wird in der Regel eine sich drehende, relativ lange Schweltrommel eingesetzt, die innen eine Vielzahl von parallelen Heizrohren aufweist, an denen der Abfall weitgehend unter Luftabschluß aufgeheizt wird. Die Schweltrommel dreht sich dabei um ihre Längsachse. Vorzugsweise ist die Längsachse etwas gegenüber der Horizontalen geneigt, so daß sich das feste Schwelgut am Ausgang der Schweltrommel ansammeln und von dort über ein Austragsrohr ausgetragen werden kann. Beim Drehen wird der Abfall durch die Heizrohre emporgehoben und fällt wieder herab. Hierdurch und durch nachrückenden Abfall wird der Transport des Festguts (Staub, Brocken aus Kohlenstoff (Koks), Steine, Flaschen-, Metall-, Keramik-Teile, etc.) in Richtung auf die Austragsöffnung der Schweltrommel bewerkstelligt.As a smoldering chamber (pyrolysis reactor) is usually one rotating, relatively long smoldering drum used has a large number of parallel heating pipes on the inside where the waste is largely heated in the absence of air becomes. The smoldering drum rotates about its longitudinal axis. The longitudinal axis is preferably somewhat opposite the horizontal inclined so that the solid char at the exit of the Collect the smoldering drum and from there via a discharge pipe can be carried out. When turning the waste through the heating pipes are lifted up and fall down again. Hereby and by moving waste becomes the transport of the solid (Dust, chunks of carbon (coke), stones, bottles, Metal, ceramic parts, etc.) towards the Discharge opening of the smoldering drum accomplished.
Wichtig bei einer solchen Heizkammer, insbesondere beim Verschwelen von Abfall, ist es, daß durch die einzelnen Heizrohre möglichst viel Heizfläche zur Verfügung gestellt wird. Um dieses zu bewirken, waren bisher im Stand der Technik Reihen von einzelnen Heizrohren vorgesehen, die sich - im Querschnitt der Schweltrommel gesehen - insbesondere geradlinig von der Innenwand der Schweltrommel in Richtung auf den Innenraum erstreckten. Zusätzlich waren im Stand der Technik gelegentlich auf und entlang der Innenwand Heizrohre ("periphere Heizrohre") angeordnet, allerdings nur nach Bedarf. Auf keinen Fall war bisher ein praktisch geschlossener Rohrkreis, das heißt ein Rohrkreis ohne Lücken, vorgesehen. Die periphere Anordnung der - unter Umständen unregelmäßig beabstandeten - Heizrohre konnte beispielsweise eine Lücke aufweisen an der Stelle, an der eine Möglichkeit zur Begehung der Schweltrommel bestand, beispielsweise durch Anordnung eines Mannloches. Außerdem ist anzumerken, daß der Abstand zwischen zwei benachbarten Heizrohren an der Innenwand bisher praktisch beliebig war. Das heißt dieser Abstand war konstruktiv bedingt und eine Funktion der erforderlichen Heizflache.Important with such a heating chamber, especially when charring of waste, it is that through the individual heating pipes as much heating area as possible is made available. Around To accomplish this have been ranks in the prior art provided by individual heating pipes, which - in cross section seen the smoldering drum - especially straight from the inner wall of the smoldering drum towards the interior extended. In addition, were in the prior art occasionally on and along the inner wall heating pipes ("peripheral heating pipes") arranged, but only as needed. In no case has it been practically closed Pipe circle, that is, a pipe circle without gaps. The peripheral arrangement of the - possibly irregular spaced - for example, heating pipes could leave a gap exhibit at the point where there is an opportunity to inspect the smoldering drum existed, for example by arranging one Manhole. It should also be noted that the distance between two neighboring heating pipes on the inner wall so far was practically arbitrary. That means this distance was constructive conditional and a function of the required heating surface.
Die Folge dieser unregelmäßigen Anordnung der Heizrohre an der Innenwand war eine Belastung des Schweltrommel-Mantels durch herabfallende Abfall-Teile. Darüber hinaus konnten sich Metallteile oder andere Festkörper-Brocken zwischen der Trommelwand und den unmittelbar benachbarten Heizrohren festklemmen. Damit war die zur Verfügung stehende Heizfläche reduziert.The consequence of this irregular arrangement of the heating pipes the inner wall was a load on the smoldering drum jacket due to falling waste parts. Beyond that could Metal parts or other solid pieces between the drum wall and clamp the directly adjacent heating pipes. This reduced the available heating area.
Aufgabe der vorliegenden Erfindung ist es, eine Heizkammer der eingangs genannten Art derart auszugestalten, daß im Bereich der Innenwand der Heizkammer eine ausreichend große Heizfläche in Form von Heizrohren für die Beheizung oder Pyrolyse des aufgegebenen Abfalls zur Verfügung steht. Mit anderen Worten: Die Gefahr des Festklemmens von Metallteilen und anderen Festkörper-Brocken soll stark vermindert werden, so daß die der Innenwand der Heizkammer zugewandte Seite der einzelnen Heizrohre für die Wärmeübertragung optimal genutzt werden kann.The object of the present invention is a heating chamber of the type mentioned in such a way that in the area a sufficiently large inside wall of the heating chamber Heating surface in the form of heating pipes for heating or pyrolysis of the discarded waste is available. With others Words: The risk of metal parts jamming and other solid chunks should be greatly reduced, so that the side facing the inner wall of the heating chamber individual heating tubes optimally used for heat transfer can be.
Diese Aufgabe wird erfindungsgemäß dadurch gelost, daß die Heizrohre - im Querschnitt gesehen - in einer praktisch geschlossenen Reihe entlang der Wand des Innenraums angeordnet sind, und daß der Abstand der Heizrohre (12b) von der Wand des Innenraumes (13) und der gegenseitige Abstand der Heizrohre (12b) kleiner als die Hälfte des Durchmessers eines Heizrohres (12b) ist.This object is achieved in that the Heating pipes - seen in cross section - in a practically closed one Row arranged along the wall of the interior are, and that the distance of the heating pipes (12b) from the wall of the Interior (13) and the mutual distance between the heating tubes (12b) smaller than is half the diameter of a heating tube (12b).
Die Erfindung beruht somit auf der Überlegung, daß sich die Verfügbarkeit einer hohen Heizfläche dadurch gewährleisten läßt, daß die einzelnen Heizrohre an der Innenwand möglichst dicht angeordnet werden. Mit anderen Worten: Um zu verhindern, daß sich die genannten Brocken im Zwischenraum festklemmen können, sollen die Heizrohre an der Trommelinnenwand einen praktisch geschlossenen Mantel, bei einer zylindrischen Schweltrommel also einen Rohrkreis bilden. Die Abstände zwischen den einzelnen Heizrohren sollen dabei so eng wie möglich gewählt werden.The invention is therefore based on the consideration that the Ensure availability of a high heating surface lets that the individual heating pipes on the inner wall if possible be arranged closely. In other words, to prevent that the chunks mentioned get stuck in the space the heating pipes on the inside of the drum a practically closed jacket, with a cylindrical one So smolder drum form a tube circle. The distances between the individual heating pipes should be as narrow as possible to get voted.
Es soll noch einmal betont werden: Durch die Anordnung eines praktisch geschlossenen, zum Beispiel kreisförmigen, Bündels wird erreicht, daß kein grobes Material durch die Zwischenräume zwischen den einzelnen Heizrohren auf die Innenwand der Heizkammer fallen und diese erodieren oder belasten kann. Es wird dadurch also sichergestellt, daß lediglich das feine Abfall-Material zwischen diesen Lücken hindurch auf die Innenwand der Heizkammer fällt. Dadurch ist auch erreicht, daß sich keine Metall-Abfallteile oder andere Festkörper-Brocken zwischen den einzelnen Heizrohren und der Innenwand verklemmen können. Somit steht lediglich das Feingut und das im Innenraum befindliche Gas in einem thermischen Kontakt mit der dem Innenmantel zugewandten Seite der einzelnen Heizrohre.It should be emphasized again: by arranging one practically closed, for example circular, bundle it is achieved that no coarse material through the gaps between the individual heating pipes on the inner wall of the Heating chamber can fall and erode or burden it. It is thus ensured that only the fine waste material between these gaps on the inner wall the heating chamber falls. This also ensures that no metal waste or other solid chunks jam between the individual heating pipes and the inner wall can. So only the fine goods and that is in the interior gas in thermal contact with the the inner jacket side of the individual heating tubes.
Zusammenfassend sind also die wesentlichen Vorteile darin zu sehen, daß lediglich feines Abfall-Material auf die Innenwand der Heizkammer fallen kann, und daß diese Innenwand mechanisch praktisch nicht belastet wird. Weiterhin ergibt sich bei einem Pyrolysereaktor oder einer Schweltrommel ein guter Wärmeaustausch von den Heizrohren in die Gasatmosphäre und in die Feingutschicht. Die Wärme, die von den Heizrohren radial nach außen abgestrahlt wird, wird somit sehr gut ausgenutzt.In summary, the main advantages are there too see that only fine waste material on the inner wall the heating chamber can fall, and that this inner wall mechanically is practically not burdened. It also follows a good one for a pyrolysis reactor or a smoldering drum Heat exchange from the heating pipes into the gas atmosphere and in the fines layer. The heat radially from the heating pipes is emitted to the outside, is therefore used very well.
Gemäß einer Weiterbildung können die an der Innenwand der Heizkammer sich befindenden Heizrohre geschützt werden gegen herabfallendes Grobgut durch sogenannte Prall-Schalen aus einem resistenten Material. Hierbei handelt es sich insbesondere um halbzylindrische Schalen. Ein solcher Schutz kann auch für Heizrohre vorgesehen sein, die sich - auf geraden oder gekrümmten Linien (im Querschnitt gesehen) - in das Innere der Heizkammer hinein erstrecken.According to a development, the on the inner wall of the Heating chamber located heating pipes are protected against falling coarse material from so-called impact shells from one resistant material. This is in particular around semi-cylindrical shells. Such protection can also be provided for heating pipes that are - on straight or curved lines (seen in cross section) - inside extend into the heating chamber.
Zum Einstieg in die Heizkammer wird man in der Regel ein Mannloch vorsehen. Bevorzugt ist nun gemäß einer weiteren Ausbildung vorgesehen, daß - gegebenenfalls im Bereich eines solchen Mannloches - Blindrohre (Dummies) in die Reihe der Heizrohre eingesetzt sind. Diese Blindrohre sind Rohre, die nicht von einem Heizgas durchströmt sind. Sie werden bevorzugt leicht demontierbar angeordnet. Damit ist erreicht, daß bei Betrieb der Heizkammer die Reihe der Heizrohre an der Innenwand geschlossen ist, während sie bei Begehung durch das Personal im Bereich des Mannloches durch Demontage der Blindrohre unterbrochen ist. To get started in the heating chamber, one is usually one Provide manhole. According to another, preference is now given Training provided that - if necessary in the area of a such manhole blind pipes (dummies) in the series of Heating pipes are used. These dummy pipes are pipes that are not flowed through by a heating gas. You are preferred arranged easily removable. This means that when the heating chamber is in operation, the row of heating pipes on the inner wall is closed while being inspected by the Personnel in the area of the manhole by dismantling the dummy pipes is interrupted.
In der Praxis hat sich gezeigt, daß ein Abstand zwischen zwei benachbarten peripheren Heizrohren und/oder Blindrohren im Bereich von 20 bis 40 mm konstruktiv möglich und gut geeignet ist.In practice it has been shown that a distance between two neighboring peripheral Heating pipes and / or blind pipes in the range from 20 to 40 mm are possible and is well suited.
Die voranstehend erwähnten Blindrohre sollten denselben Durchmesser haben wie die an der Innenwand angeordneten peripheren Heizrohre.The blind pipes mentioned above should be the same Have diameters like the peripheral ones arranged on the inner wall Heating pipes.
Der Abstand des (bevorzugt geschlossenen) Rohrkreises von der Innenwand der Heizkammer sollte möglichst gering sein. Er wird in der Regel durch konstruktive Vorgaben bestimmt sein, beispielsweise durch die Befestigung der Heiz- und/oder Blindrohre an Endplatten. Üblicherweise kann dieser Abstand im Bereich zwischen 20 bis 40 mm liegen.The distance of the (preferably closed) pipe circle from the The inner wall of the heating chamber should be as small as possible. He will usually be determined by design specifications, for example by attaching the heating and / or Blind pipes on end plates. Usually this distance can are between 20 and 40 mm.
Ausführungsbeispiele der Erfindung werden im folgenden anhand
von drei Figuren näher erläutert. Es zeigen:
Nach Figur 1 wird fester Abfall A über eine Zufuhr- oder Aufgabeeinrichtung
2 mit Fallschacht 3 und über eine Schnecke 4,
die von einem Motor 6 angetrieben wird und in einem Aufgaberohr
7 angeordnet ist, zentral in einen Pyrolysereaktor oder
eine Schwelkammer 8 eingebracht. Die Schwelkammer 8 ist im
Ausführungsbeispiel eine innenbeheizbare, um ihre Längsachse
10 drehbare Schwel- oder Pyrolysetrommel, die eine Länge von
15 bis 30 m besitzen kann, die bei 300 bis 600 °C arbeitet,
die weitgehend unter Sauerstoffabschluß betrieben wird und
die neben flüchtigem Schwelgas s einen weitgehend festen Pyrolysereststoff
erzeugt. Es handelt sich dabei um eine innenberohrte
Schweltrommel 8 mit einer Vielzahl (zum Beispiel
50 bis 200) von parallel zueinander ausgerichteten Heizrohren
12, von denen in Figur 1 nur vier gezeigt sind, die im Innenraum
13 angeordnet sind. Am rechten oder "heißen" Ende ist
ein Einlaß für Heizgas h in Form einer ruhenden, abgedichteten
Heizgas-Einlaßkammer 14 vorgesehen, und am linken oder
"kalten" Ende ist ein Auslaß für das Heizgas h in Form einer
ruhenden, abgedichteten Heizgas-Auslaßkammer 16 angeordnet.
Die Längsachse 10 der Schweltrommel 8 ist bevorzugt gegenüber
der Horizontalen geneigt, so daß der Auslaß am rechts gelegenen
"heißen" Ende tiefer liegt als der links gezeigte Einlaß
für den Abfall A. Die Schweltrommel 8 ist bevorzugt auf
leichten Unterdruck gegenüber der Umgebung gehalten.According to Figure 1, solid waste A via a feed or
Die Pyrolysetrommel 8 ist ausgangs- oder austragsseitig über
ein sich mitdrehendes zentrales Austragsrohr 17 eine Austragsvorrichtung
18 nachgeschaltet, die mit einem Schwelgas-Abzugsstutzen
20 für den Abgang des Schwelgases s und mit einem
Pyrolysereststoffausgang 22 für die Abgabe des festen Pyrolysereststoffes
f versehen ist. Eine an den Schwelgas-Abzugsstutzen
20 angeschlossene Schwelgasleitung ist mit dem
Brenner einer (nicht gezeigten) Hochtemperatur-Brennkammer
verbunden.The pyrolysis drum 8 is on the output or discharge side
a rotating central discharge pipe 17 a
Die Drehbewegung der Schweltrommel 8 um ihre Längsachse 10
wird durch einen Antrieb 24 in Form eines Getriebes bewirkt,
der an einen Motor 26 angeschlossen ist. Die Antriebsmittel
24, 26 arbeiten zum Beispiel auf einem Zahnkranz, der am Umfang
der Schweltrommel 8 befestigt ist. Die Lager der Schweltrommel
8 sind mit 27 bezeichnet.The rotational movement of the smoldering drum 8 about its
Aus Figur 1 wird deutlich, daß die Heizrohre 12 jeweils mit
ihrem einen Ende an einer ersten Endplatte 28 und mit ihrem
anderen Ende an einer zweiten Endplatte 30 befestigt sind.
Die Befestigung an den Endplatten 28, 30 ist so getroffen,
daß sich bevorzugt eine leichte Austauschbarkeit der Heizrohre
12 ergibt. Das Ende der Heizrohre 12 ragt jeweils durch
eine Öffnung aus dem Innenraum 13 nach links in die Auslaßkammer
16 bzw. nach rechts in die Einlaßkammer 14 hinein. Die
Achse der Heizrohre 12 ist dabei jeweils senkrecht zur Oberfläche
der Endplatten 28, 30 ausgerichtet. Bei der gezeigten
Konstruktion ist beachtet, daß die einzelnen Heizrohre 12
thermisch und mechanisch hoch beansprucht sind, und daß sich
die Endplatten 28, 30, die auch als Rohrplatten oder Trommelrohrböden
bezeichnet werden konnten, um die Längsachse 10 der
Schweltrommel 8 mitdrehen.From Figure 1 it is clear that the
Zwischen den Endplatten 28, 30 sind zwei Stützstellen X, Y
zum Stützen der (andernfalls möglicherweise durchhängenden)
Heizrohre 12 vorgesehen. In Transportrichtung des Abfalls A
gesehen liegt die erste Stützstelle X etwa bei einem Drittel
(1/3 1) und die zweite Stützstelle Y etwa bei zwei Dritteln
(2/3 1) der Gesamtlänge 1 der Schweltrommel 8. Hier sind
Trag- oder Stützkonsolen 31, 32 in Form von gerundeten Lochplatten
aus Metall, zum Beispiel aus Stahl, vorgesehen. Sie
sind an der Innenwand 33 befestigt.Between the
Die Heizrohre 12 können in einer Konfiguration angeordnet
sein, wie sie in Figur 2 sowie in Figur 3 dargestellt ist.
Danach gibt es eine Vielzahl peripher angeordneter Heizrohre
12b und eine Vielzahl entlang gekrümmter bzw. gerader Linien
angeordneter Heizrohre 12a zur Beheizung des mehr zentral
liegenden Abfalls. Die Krümmung richtet sich nach der Drehung
der Schweltrommel 8, die durch einen Pfeil 35 angedeutet ist.The
Aus Figur 2 wird deutlich, daß sechs kürzere und sechs längere
nicht-radiale Reihen von innenliegenden Heizrohren 12a
vorgesehen sind. Die peripheren Heizrohre 12b befinden sich
auf einem praktisch lückenlosen oder geschlossenen Kreis nahe
der Innenwand 33 der Schweltrommel 8. From Figure 2 it is clear that six shorter and six longer
non-radial rows of
Die nicht-radialen Reihen beginnen gemäß Figuren 2 und 3 jeweils
im Bereich der Innenwand 33. Sie sind - und das ist von
besonderer Bedeutung - entgegen der Drehrichtung 35 gekrümmt
(vergleiche Figur 2) bzw. geneigt (vergleiche Figur 3). Dadurch
ist gewährleistet, daß bei der Drehung um die Langsachse
10 sich auf den Heizrohren 12a, 12b ansammelnder Abfall A
frühzeitig herabfallen und damit keine nennenswerte Fallhöhe
erreichen kann. Damit wird die Gefahr der Beschädigung durch
im Abfall A enthaltener Brocken wirksam reduziert.The non-radial rows start according to FIGS. 2 and 3, respectively
in the area of the
Zur Verdeutlichung ist in Figur 3 ein stumpfer Winkel α bezüglich der Ausrichtung der einzelnen Reihen zur Tangente an die Wand der Schweltrommel 8 eingetragen.For clarification, an obtuse angle α is shown in FIG the alignment of the individual rows to the tangent entered the wall of the smoldering drum 8.
Zur guten Verschwelung des Abfalls A ist auch vorgesehen, daß
der gegenseitige Abstand der einzelnen Heizrohre 12a weniger
als der halbe Durchmesser eines Heizrohres 12a der betreffenden
Reihe beträgt. Dies gilt auch für die peripheren Heizrohre
12b.For good smoldering of waste A it is also provided that
the mutual distance between the
In Figur 3 sind an einer einzigen linearen Reihe Schutz- oder
Prallschalen 40 eingezeichnet. Die restlichen linearen Reihen
werden - ebenso wie die gekrümmten Reihen der Heizrohre 12a
in Figur 2 - der Zentralachse 10 zugewandt ebenfalls mit solchen
Prallschalen 40 aus resistentem Material belegt sein.
Entsprechenden gilt für Prallschalen 50, die für die peripheren
Heizrohre 12b in den Figuren 2 und 3 vorgesehen sein können.
Von diesen Prallschalen 50 sind der Übersichtlichkeit
wegen in Figur 3 nur zwei gezeigt.In Figure 3 are on a single linear row protection or
Baffles 40 shown. The remaining linear rows
as well as the curved rows of
In Figur 3 ist noch gezeigt, daß im Bereich eines schematisch
dargestellten Mannloches 60, durch das bei Wartungs- oder Reparaturarbeiten
Personal in den Innenraum 13 einsteigen kann,
die kreisringförmige Reihe der Heizrohre 12b durch Blindrohre
12D gleicher Lange und gleichen Außendurchmessers vollständig
ergänzt ist. Diese Blindrohre 12D sind an den Endplatten 28,
30 leicht lösbar befestigt. Im Wartungs- oder Reparaturfall
werden sie entfernt. Im Betrieb sorgen alle Rohre 12b, 12D
dafür, daß nur Feingut an die Innenwand 33 gelangen kann.
Insgesamt gesehen sind die Rohre 12a, 12D auf einem praktisch
lückenlos geschlossenen Kreisring eng benachbart angeordnet.In Figure 3 it is also shown that in the area of a schematic
illustrated
Claims (5)
- Heating chamber for solid material, which chamber is rotatable about its longitudinal axis (10), preferably a low-temperature carbonization drum (8) for waste (W), having a number of heating tubes (12b) accommodated in the interior space (13) and aligned approximately parallel to one another, characterized in that the heating tubes (12b), viewed in cross-section, are arranged along the wall (33) of the interior space (13) and that the spacing of the heating tubes (12b) from the wall of the interior space (13) and the mutual spacing of the heating tubes (12b) is less than half the diameter of a heating tube (12b).
- Heating chamber according to Claim 1, characterized in that the spacing of the heating tubes (12b) from the wall of the interior space (13) is between 20 mm and 40 mm.
- Heating chamber according to Claim 1 or 2, characterized in that the mutual spacing of the heating tubes (12b) is between 20 mm and 40 mm.
- Heating chamber according to any one of Claims 1 to 3, characterized in that dummies (12D) which are easy to remove are arranged in place of some heating tubes (12b).
- Heating chamber according to Claim 4, characterized in that the dummies (12D) have the same diameter as the heating tubes (12b).
Applications Claiming Priority (5)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE4329871A DE4329871A1 (en) | 1993-09-03 | 1993-09-03 | Pipe-rotatable heating chamber for waste |
DE4329871 | 1993-09-03 | ||
DE4429897 | 1994-08-23 | ||
DE19944429897 DE4429897A1 (en) | 1994-08-23 | 1994-08-23 | Rotary heating chamber esp. for waste pyrolysis |
PCT/DE1994/000996 WO1995006698A1 (en) | 1993-09-03 | 1994-08-30 | Rotary heating chamber for solids |
Publications (3)
Publication Number | Publication Date |
---|---|
EP0716676A1 EP0716676A1 (en) | 1996-06-19 |
EP0716676B1 true EP0716676B1 (en) | 1998-05-20 |
EP0716676B2 EP0716676B2 (en) | 2001-08-22 |
Family
ID=25929219
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP94924703A Expired - Lifetime EP0716676B2 (en) | 1993-09-03 | 1994-08-30 | Rotary heating chamber for solids |
Country Status (17)
Country | Link |
---|---|
US (1) | US5716205A (en) |
EP (1) | EP0716676B2 (en) |
JP (1) | JP2789559B2 (en) |
KR (1) | KR100304305B1 (en) |
CN (1) | CN1076042C (en) |
AT (1) | ATE166380T1 (en) |
CA (1) | CA2170908A1 (en) |
CZ (1) | CZ53296A3 (en) |
DE (1) | DE59406041D1 (en) |
DK (1) | DK0716676T4 (en) |
ES (1) | ES2116609T5 (en) |
HU (1) | HU218442B (en) |
PL (1) | PL313146A1 (en) |
RU (1) | RU2124036C1 (en) |
SK (1) | SK281940B6 (en) |
TW (1) | TW287223B (en) |
WO (1) | WO1995006698A1 (en) |
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GB9705338D0 (en) * | 1997-03-14 | 1997-04-30 | Thames Water Utilities | A process and apparatus for treating as gas |
US5997288A (en) * | 1997-04-18 | 1999-12-07 | Robert J. Adams | Apparatus for thermal removal of surface and inherent moisture and limiting rehydration in high moisture coals |
DE19726150C1 (en) * | 1997-06-19 | 1998-11-05 | Siemens Ag | Rotary waste pyrolysis drum |
ES2186610T3 (en) * | 2000-12-15 | 2003-05-16 | Cleanaway Deutschland Ag & Co | DEVICE FOR PURIFYING AND / OR DECONTAMINATING POLYESTERS. |
US6808602B2 (en) * | 2001-04-25 | 2004-10-26 | Conocophillips Company | Coke drum bottom head removal system |
KR100722333B1 (en) * | 2004-04-14 | 2007-06-04 | 주식회사 한국종합플랜트 | Thermal cracking equipment |
US7550063B2 (en) * | 2005-08-26 | 2009-06-23 | Altene (Canada) Inc. | Method and apparatus for cracking hydrocarbons |
US7545725B2 (en) | 2005-12-06 | 2009-06-09 | Daxon Technology Inc. | Optical reading apparatus capable of correcting aberration |
JP5184943B2 (en) * | 2008-03-31 | 2013-04-17 | 三井造船株式会社 | Indirect heating type thermal decomposition equipment |
CN101985562B (en) * | 2010-08-19 | 2011-09-14 | 西峡龙成特种材料有限公司 | Horizontal coal separating equipment with multiple combustors |
CN101985558B (en) * | 2010-08-19 | 2012-01-04 | 西峡龙成特种材料有限公司 | Coal decomposing equipment |
US8342433B2 (en) | 2010-10-12 | 2013-01-01 | Landis Kevin C | Apparatus and method for processing recyclable asphalt materials |
CN101984022B (en) * | 2010-10-26 | 2011-08-10 | 西峡龙成特种材料有限公司 | External heating coal decomposing equipment with multiple pipes |
US8960108B1 (en) | 2010-12-20 | 2015-02-24 | SilverStreet Group, LLC | System and method for cogeneration from mixed oil and inert solids, furnace and fuel nozzle for the same |
CN103588377A (en) * | 2013-11-19 | 2014-02-19 | 合肥环坤污泥干化设备有限公司 | Sludge drying equipment |
US9932524B1 (en) * | 2014-02-03 | 2018-04-03 | Modern Recovery Systems, Inc. | Method, apparatus and system for processing materials for recovery of constituent components |
US10676674B1 (en) | 2014-02-03 | 2020-06-09 | Modern Recovery Systems, Inc. | Method, apparatus and system for processing materials for recovery of constituent components and use of such components in asphalt |
UA119005C2 (en) * | 2015-04-02 | 2019-04-10 | Бті Гумковскі Сп. З О.О. Сп. К. | Solid fuel boiler burner |
CN104864688B (en) * | 2015-05-29 | 2017-05-17 | 山东天力能源股份有限公司 | Large multi-tube diffusion airflow rotary dryer and drying method |
CN106753488A (en) * | 2016-12-12 | 2017-05-31 | 朱书红 | Material heater |
CN109355068B (en) * | 2018-10-17 | 2020-08-04 | 广州市挂绿环保工程有限公司 | Pyrolysis furnace |
CN110630219B (en) * | 2019-08-27 | 2022-03-15 | 河北迪运化工科技有限公司 | Kiln for burning oil-containing mixture at high temperature |
KR102257066B1 (en) * | 2020-04-29 | 2021-06-09 | 새마을환경개발주식회사 | Drying furnace using waste heat of the firing process in the manufacture of high-strength mortar sand as a firing process and the recycling of sludge generated during the manufacturing process as a cement raw material |
CN114166019A (en) * | 2021-11-10 | 2022-03-11 | 湖南德景源科技有限公司 | Powder material sintering furnace |
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-
1994
- 1994-08-30 CA CA002170908A patent/CA2170908A1/en not_active Abandoned
- 1994-08-30 AT AT94924703T patent/ATE166380T1/en not_active IP Right Cessation
- 1994-08-30 HU HU9600523A patent/HU218442B/en not_active IP Right Cessation
- 1994-08-30 CZ CZ96532A patent/CZ53296A3/en unknown
- 1994-08-30 WO PCT/DE1994/000996 patent/WO1995006698A1/en not_active Application Discontinuation
- 1994-08-30 SK SK277-96A patent/SK281940B6/en unknown
- 1994-08-30 DE DE59406041T patent/DE59406041D1/en not_active Expired - Fee Related
- 1994-08-30 JP JP7507872A patent/JP2789559B2/en not_active Expired - Fee Related
- 1994-08-30 CN CN94193277A patent/CN1076042C/en not_active Expired - Fee Related
- 1994-08-30 DK DK94924703T patent/DK0716676T4/en active
- 1994-08-30 RU RU96107102A patent/RU2124036C1/en active
- 1994-08-30 ES ES94924703T patent/ES2116609T5/en not_active Expired - Lifetime
- 1994-08-30 EP EP94924703A patent/EP0716676B2/en not_active Expired - Lifetime
- 1994-08-30 KR KR1019960701066A patent/KR100304305B1/en not_active IP Right Cessation
- 1994-08-30 PL PL94313146A patent/PL313146A1/en unknown
- 1994-09-17 TW TW083108705A patent/TW287223B/zh active
-
1996
- 1996-03-04 US US08/610,520 patent/US5716205A/en not_active Expired - Fee Related
Also Published As
Publication number | Publication date |
---|---|
CA2170908A1 (en) | 1995-03-09 |
JP2789559B2 (en) | 1998-08-20 |
RU2124036C1 (en) | 1998-12-27 |
WO1995006698A1 (en) | 1995-03-09 |
US5716205A (en) | 1998-02-10 |
DK0716676T4 (en) | 2001-10-01 |
HUT72953A (en) | 1996-06-28 |
PL313146A1 (en) | 1996-06-10 |
ES2116609T5 (en) | 2002-01-16 |
JPH08510502A (en) | 1996-11-05 |
KR960704997A (en) | 1996-10-09 |
DE59406041D1 (en) | 1998-06-25 |
KR100304305B1 (en) | 2001-11-22 |
CN1076042C (en) | 2001-12-12 |
TW287223B (en) | 1996-10-01 |
DK0716676T3 (en) | 1999-03-08 |
SK27796A3 (en) | 1997-07-09 |
EP0716676B2 (en) | 2001-08-22 |
HU218442B (en) | 2000-08-28 |
CZ53296A3 (en) | 1996-06-12 |
EP0716676A1 (en) | 1996-06-19 |
HU9600523D0 (en) | 1996-04-29 |
ATE166380T1 (en) | 1998-06-15 |
ES2116609T3 (en) | 1998-07-16 |
CN1130394A (en) | 1996-09-04 |
SK281940B6 (en) | 2001-09-11 |
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