EP1144137B1 - Sieving device for solid material and a method for sieving solid material - Google Patents

Sieving device for solid material and a method for sieving solid material Download PDF

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Publication number
EP1144137B1
EP1144137B1 EP99936263A EP99936263A EP1144137B1 EP 1144137 B1 EP1144137 B1 EP 1144137B1 EP 99936263 A EP99936263 A EP 99936263A EP 99936263 A EP99936263 A EP 99936263A EP 1144137 B1 EP1144137 B1 EP 1144137B1
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EP
European Patent Office
Prior art keywords
rod
screening device
refuse
spiral
solid residues
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
Application number
EP99936263A
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German (de)
French (fr)
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EP1144137A2 (en
EP1144137A3 (en
Inventor
Helmut Werdinig
Winfried Von Rhein
Reinhold Riggenmann
Georg Gropper
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Takuma Co Ltd
Mitsui Engineering and Shipbuilding Co Ltd
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Siemens AG
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Publication date
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Priority to EP03011845A priority Critical patent/EP1348492B1/en
Priority to DK03011845T priority patent/DK1348492T3/en
Publication of EP1144137A2 publication Critical patent/EP1144137A2/en
Publication of EP1144137A3 publication Critical patent/EP1144137A3/en
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Publication of EP1144137B1 publication Critical patent/EP1144137B1/en
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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B07SEPARATING SOLIDS FROM SOLIDS; SORTING
    • B07BSEPARATING SOLIDS FROM SOLIDS BY SIEVING, SCREENING, SIFTING OR BY USING GAS CURRENTS; SEPARATING BY OTHER DRY METHODS APPLICABLE TO BULK MATERIAL, e.g. LOOSE ARTICLES FIT TO BE HANDLED LIKE BULK MATERIAL
    • B07B1/00Sieving, screening, sifting, or sorting solid materials using networks, gratings, grids, or the like
    • B07B1/18Drum screens
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10BDESTRUCTIVE DISTILLATION OF CARBONACEOUS MATERIALS FOR PRODUCTION OF GAS, COKE, TAR, OR SIMILAR MATERIALS
    • C10B1/00Retorts
    • C10B1/10Rotary retorts
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10BDESTRUCTIVE DISTILLATION OF CARBONACEOUS MATERIALS FOR PRODUCTION OF GAS, COKE, TAR, OR SIMILAR MATERIALS
    • C10B53/00Destructive distillation, specially adapted for particular solid raw materials or solid raw materials in special form

Definitions

  • the invention relates to a pyrolysis plant according to the preamble of claim 1.
  • Thermal processes are known for waste disposal, at where the waste is burned in waste incineration plants or in Pyrolysis plants pyrolyzed, i.e. in the absence of air Temperature from about 400 ° C to 700 ° C is subjected. at Both methods make sense after the combustion or to separate the residue remaining after pyrolysis, to either recycle it or dispose of it in a suitable manner. The aim is to residual material to be disposed of in a landfill as low as possible to keep.
  • the pyrolysis residue also has non-combustible parts.
  • the non-combustible parts essentially consists of an inert fraction, such as glass, Stones or ceramics, as well as composed of a metal fraction.
  • the recyclable materials are sorted out and recycled fed. There are procedures for sorting out and components necessary that are reliable and continuous Ensure operation.
  • the problem with screening devices is often that clog the sieve surfaces. Then the screening device fails, or it must at least be a complex and labor-intensive one Undergo cleaning.
  • the problem of constipation the screening device occurs particularly in the case of a strongly inhomogeneous Composition of the solid to be separated. So for example, wires get caught in screen surfaces Perforated sheets, so that the individual holes first be narrowed and clog up over time.
  • the residue obtained during pyrolysis is typical such a strongly inhomogeneous solid, which with regard to its material composition, its size and geometry its solid parts shows great differences.
  • the residue is next to stones, broken glass and larger metal parts also elongated bars as well as in twisted wires (wire bulges).
  • a discharge device for pyrolysis residues known from a smoldering drum includes a conveyor that has a sawtooth profiled partition with an attached Rod screen has.
  • the partition will vibrate offset so that the fine of the separate coarse parts. The fine parts fall through subsequent rod sieve through, while the coarse fractions slide on the bar screen. Wirewalls can however, hang on the poles and cause constipation to lead.
  • EP 0 086 488 A2 also includes a pyrolysis plant for waste known a screening device for solid, the screening device is rotatable about its longitudinal axis.
  • FR 27 45 204 A1 also discloses the use a rod wound along a helix at one Screening device.
  • the present invention has for its object a Pyrolysis plant for waste with a sieve for solid Specify residual material in the case of continuous operation with simple means is guaranteed without constipation occur.
  • the rod member is substantially parallel to that formed by the spiral outer surface or parallel to the formed by the multi-course screen and acts as a wiping element as follows: a wire bulge gets caught on the pole, this wire bulge is due to the Rotary movement of the sieve against the fixed rod element out and is guided by this along the helix of stripped the rod. To achieve this is the sense of rotation the rod to the direction of rotation of the screening device switched off.
  • the rod is a spiral with several turns, in particular with about four to ten Turns, formed.
  • a screening device which is also called a "spiral screen”
  • the solid to be sieved into the interior formed by the three-dimensional spiral brought in Fine solid with smaller dimensions as the distance between two turns of the spiral falls through the spiral while coarse solid in the interior is further promoted.
  • Spacing between turns can be the maximum size of the sieved finer solids content can be adjusted.
  • a major advantage of the spiral is that any waste parts stuck between two turns be lifted up by the rotary movement and in particular fall at the upper turning point due to their own weight.
  • the simple and robust design of the screening device as a spiral therefore, avoids permanent constipation and enables continuous operation.
  • a number of rods are in a practical embodiment provided, the rod beginnings arranged rotatably are. Each bar runs along a helix. Such a sieve with several rods is also called multi-pass sieve.
  • the angle of rotation of the rods is less than 360 °. In particular is the angle of rotation is less than or approximately equal to 180 °.
  • the rod element is for the most efficient stripping preferably also wound along a helix, and in particular counter to the rod, so that it with the rod, for example, an angle of preferred 90 ° includes.
  • the spiral screen the spiral is attached to only one of its two ends, so that the spiral axis due to its own weight towards its gravity towards its unpaved end is curved below.
  • the spiral is preferred only at the beginning of the spiral held while the spiral end located in the conveying direction is designed to hang freely.
  • the main advantage of curvature is that that the distances of the turns at the bottom of the spiral are smaller than the distances at the top of the spiral.
  • Solid matter introduced into the spiral can in principle only between turns on the lower side of the spiral jam because as soon as it is lifted due to its Dead weight falls down. In other words: through the Spiral movement becomes a jammed solid part with the Spiral raised up. At the same time, the distance is widening of the turns so that the solid part between the turns cannot remain clamped and due to its own weight inevitably falls down.
  • the screening device with curved spiral is therefore highly self-cleaning.
  • a such a spiral is extremely robust and is particularly suitable also for rough separation of heavy and large solids.
  • the spiral is made of plastic, for example.
  • an alignment device is provided in the screening device, which is arranged in the conveying direction in front of the rod, and the flows into the interior.
  • the alignment of the elongated solid parts ensures that this is essentially parallel to the longitudinal axis in the interior can be introduced. Elongated solid parts are therefore also automatically as coarse solid parts treated and promoted. You can't be vertical fall through the spiral to the longitudinal axis. Consequently is guaranteed that by the off the shelf or by the The sieve formed from rods only falls through solid particles, whose largest dimension is smaller than the distance two turns of the spiral or as the distance between two Rods.
  • the alignment device is as one configured drum rotatable about its longitudinal axis. by virtue of the solid parts are aligned with the rotary movement of the drum automatically in the direction of the drum axis.
  • the helix is particularly immediately on arranged on the inlet side of the drum and has a relative high flank.
  • the helix is in particular designed such that it - in a plan view seen in the direction of the longitudinal axis of the drum - forms a closed circle. This means that that solids on the drum bottom straight from the drum entrance slide through to the drum exit without any obstacles can. In order not to obstruct the flow of solids unnecessarily, becomes a multi-turn helix with an angle of rotation smaller 360 ° preferred. In this case, the desired overlap the flank reaches and at the same time becomes a relatively flat one Incline of the helix allows for a faster solids transport inside the drum.
  • the alignment device as a profiled oscillating floor with longitudinal grooves designed in which the longitudinal grooves in the conveying direction run and in which the elongated solid parts due the vibrations of the vibrating floor in these longitudinal grooves be aligned.
  • the rod is advantageously on the in the conveying direction end face of the drum attached to this and there especially welded.
  • the rod is preferably attached in such a way that the drum exit in the formed by the rod Interior opens.
  • the rod is out of the drum on the outer wall of the drum or at least attached flush with the drum.
  • the screening device is in a particularly preferred embodiment with the discharge side of the smoldering drum of the pyrolysis plant for screening of those obtained from the smoldering drum Pyrolysis residues connected.
  • the Rod is, for example, directly on a discharge pipe attached to the smoldering drum and within a discharge device arranged.
  • This discharge device is preferred sealed gas-tight from the outside atmosphere to prevent entry to avoid atmospheric oxygen leading to combustion of the combustible and hot pyrolysis residue.
  • the distance between two turns of the spiral or between two rods advantageously about 100 mm to 300 mm and in particular about 180 mm.
  • the interior formed by the rod has one Length of about 0.5 to 1.5 m. Its diameter is about 1.5 m, and a sieve device with drum and sieve preferably has a total length of about 2 to 4 m. The Length of the interior is suitably less or equal to the diameter of the drum.
  • a screening device 1 comprises an alignment device, namely a drum rotatable about its longitudinal axis 2, which is inclined to the horizontal.
  • a shaft-like feeder 6 arranged for solid R. With this solid R e.g. pyrolysis residue or rubble.
  • On the right of the feeder 6 opposite Front 7 of drum 2 is one along a helix coiled rod 8 made of metal attached to a spiral 10 with an interior 11 forms.
  • the spiral 10 is for example with a suitable welding, screwing or Clamp connection attached to the drum 2.
  • the spiral 10 aligns approximately with the drum 2, so that the diameter the drum 2 and that of the spiral 10 are approximately the same.
  • the drum 2 is rotatably supported. You can't over one drive shown in detail can be set in rotation. Together the drum 2 also rotates the drum 2 attached spiral 10. This has five turns according to Figure 1 on. The distance between two adjacent turns depends on the type of solid R. It is present preferably about 180 mm.
  • the spiral wound Rod 8 is made of a robust material and is special metallic. For example, it is a round bar or a steel pipe.
  • the spiral 10 is only one-sided, namely on the drum 2 attached. Your spiral end facing away from drum 2 is free of fasteners and is not supported. The spiral 10 will therefore become unpaved Bend downward due to gravity. hereupon is discussed in more detail below in FIG. 2.
  • the solid R is the feed device 6 in the Drum 2 is given and is due to the inclination of the drum 2nd and the rotational movement in the conveying direction 14 towards the spiral 10 transported. Fine solid F is separated off in the spiral 10, while coarse solid G is transported further by the spiral 10 becomes.
  • a major advantage of the screening device 1 with the spiral 10 can be seen in the fact that even more fluent Solid R through the rotary movement in a simple manner in the conveying direction 14 is transported.
  • Figure 2 shows a schematic section through a curved Spiral 10. This is the main principle of operation of the curved spiral 10 explained.
  • the spiral axis 12 (and with it the entire spiral 10) points according to Figure 2 shows a curvature. Because of the curvature is the top one Distance o between two successive turns larger than the lower distance u between two turns.
  • On Solid part R can only be in the lower part of the spiral 10 clamp where the distance u between two turns is small.
  • a clamped solid part P is through the Rotational movement of the spiral 10 promoted upward, and at the same time the distance between the turns becomes larger, so that the Solid part P loosens and falls.
  • the smoldering drum 26 of a pyrolysis plant via a feed shaft 27 and a feed device 28 loaded with waste A.
  • the waste A is in the smoldering drum 26 at around 450 ° C. This creates a Smoldering gas S and a solid or pyrolysis residue R.
  • Die Smoldering drum 26 is preferred over not shown internal heating pipes heated. It is opposite the horizontal inclined and rotatable.
  • a discharge pipe 29 is arranged on the end the spiral 10 is attached.
  • the discharge pipe 29 and the Spiral 10 form the sieve device 1.
  • the discharge pipe 29 also serves as an alignment device for elongated Solid parts. With the spiral 10, the fine solids F separated from the coarse solids content G.
  • the discharge pipe 29 with a connected spiral 10 opens into a discharge device 30 which is opposite the rotating Smoldering drum 26 sealed gas-tight via mechanical seals 32 is.
  • the same as the discharge device 30 the feed device 28 to the smoldering drum 26 via mechanical seals 32 sealed gas-tight.
  • This is to be avoided be that atmospheric oxygen penetrates into the smoldering drum 26 and the one that runs largely oxygen-free in the smoldering drum 26 Pyrolysis process affected.
  • the carbonization gas S which via the discharge pipe 29 into the discharge device 30 flows and from there via a carbonization gas outlet 34 is derived.
  • Smoldering drum 26 With the arrangement of the spiral 10 on the discharge tube 29 Smoldering drum 26 is the pyrolysis residue R immediately after the smoldering drum 26 into a fine solid fraction F and a coarse solid content G separated. The danger of one Blockage from the smoldering drum 26 downstream components is therefore only minor.
  • the screening device is generally suitable for direct connection on rotating pipes, e.g. Rotary kilns or smoldering drums, in which the solid is subjected to treatment what it should be separated after.
  • the fine residual material F separated with the screening device 1 is preferably a so-called for further processing Subjected to wind sifting.
  • a zigzag-shaped one has proven particularly useful Exposed in the air from below and shaft the solid is fed from above or from the side.
  • FIG. 4 shows an alternative embodiment to the spiral 10 shown, in which a instead of the spiral 10 Number of rods 8 is arranged at the end of the drum 2.
  • the rods 8 are each wound along a helix and can therefore be regarded as a multi-start spiral become.
  • the individual rods 8 are at the end of each other Drum 2 preferably arranged rotatably offset by an angle of 30 °.
  • Each individual rod 8 has an angle of rotation less than 360 °, does not form a complete rotation.
  • the decisive advantage with this multi-start helix like also with the spiral 10 according to FIG. 1, there is the arrangement one or more helically wound rods 8, so that the rotary movement of the screening device 1 any stuck solid parts automatically to the end the screening device are transported further and dropped there become.
  • the rod member 35 is also in the embodiment arranged with the spiral 10, although there not shown in detail. It causes one on a pole 8 hanging solid part due to the relative movement between rod 8 and rod element 35 in conveying direction 14 is withdrawn from the rod 8. This is the direction of rotation the screening device 1 and the direction of rotation of the rods 8 on top of each other Voted.
  • the rod element 35 In order to increase the stripping effect, the rod element 35 also wound and crossed along a helix the rods 8 preferably at an angle of 90 °.
  • the slope of the rod element 35 preferably takes in the conveying direction 14 to increase the wiping effect.
  • the effect will be further improved if several rod elements 35 are provided are. For example, these are approximately semicircular below the rods 8 arranged.
  • the rod element 35 Another advantage of the arrangement of the rod element 35 can be seen in the fact that elongate solid parts 16, which are not aligned completely parallel to the longitudinal direction 3 in the drum 2, cannot fall through a gap between the rods 8. Because of the rotary movement of the drum 2, it may happen that the elongated solid parts 16 are also lifted up so that they meet the rods 8 at an acute angle at the outlet of the drum 2. It can also be seen from FIG. 4 that a multi-start spiral 36 is arranged on the inlet side of the drum 2.
  • the multi-turn helix 36 comprises two helical sheets which are arranged so as to be rotationally offset from one another. Further sheets can also be provided.
  • the coil 36 is arranged on the inside of the drum 2 and is designed in such a way that at least two coil sections overlap at each point on the drum base.
  • the flanks of the helix, i.e. the sheets, are relatively high. This ensures that the solid R introduced by the feed device 6 is braked and does not fly through or shoot through the screening device 1 without the solid R undergoing screening.
  • the multi-pass sieve with several described for FIG Rods 8 can, without limitation, the spiral sieve 10 from FIG 3 replace.
  • a pyrolysis plant according to the invention with a screening device is characterized by a very simple and robust construction while ensuring trouble-free Operation without clogging. decisive Aspects for ensuring safe operation are the design of the screening device with the helical coiled rod 8 or with the rods 8 passing through the curvature of the spiral 10 caused differences in distance of the turns, the safe separation of elongated Solid parts due to the upstream alignment device as well as that by the rotational movement and spiral movement conditional automatic transport of solid R.

Abstract

The screening device uses a rod (8) which is wound into a spiral (10). It is rotated is fed into the interior of the spiral, e.g. via a rotary feed drum (2) with the spiral attached to it at one end. The rotary feed drum may be inclined to the horizontal, with the spiral attached to its lower end. The axis of the spiral may be curved downwards due to the spiral weight.

Description

Die Erfindung betrifft eine Pyrolyseanlage gemäß dem Oberbegriff von Anspruch 1.The invention relates to a pyrolysis plant according to the preamble of claim 1.

In vielen technischen Anwendungsgebieten ist es notwendig, daß Feststoffe, die beispielsweise in Schüttgut enthalten sind, in mehrere Fraktionen getrennt werden. Die Fraktionen werden in der Regel nach unterschiedlichen Feststoffgrößen, Feststoffgeometrien oder Feststoffbeschaffenheiten unterteilt. Eine Trennung der Feststoffe ist immer dann erwünscht, wenn die unterschiedlichen Feststofffraktionen einer weiteren Behandlung zugeführt werden sollen.In many technical fields of application it is necessary that solids contained, for example, in bulk material are divided into several fractions. The factions are usually based on different solids sizes, Solid geometries or textures divided. A separation of the solids is always desirable if the different solid fractions of another Treatment should be administered.

In der Bauindustrie wird beispielsweise anfallender Bauschutt von großen und sperrigen Schuttanteilen getrennt, die dann sortiert und wiederverwertet werden. Der abgetrennte feinere Bauschutt wird beispielsweise auf einer dafür vorgesehenen Deponie entsorgt.In the construction industry, for example, there is building rubble separated from large and bulky debris, which then sorted and recycled. The separated finer Building rubble is, for example, on a designated one Landfill.

Auf dem Gebiet der Abfallentsorgung wird im Hinblick auf eine möglichst umweltschonende Entsorgung eine Trennung und Sortierung des Abfalls oder der bei der Abfallverwertung anfallenden Reststoffe immer bedeutender. Ein wesentlicher Punkt hierfür ist eine Trennung des Abfalls nach seiner Größe. Die Trennung kann vor der Verwertung des Abfalls durchgeführt werden; sie kann aber auch ein wesentlicher Verfahrensschritt bei der Abfallverwertung selbst sein.In the field of waste disposal, with regard to a disposal and sorting as environmentally friendly as possible of the waste or that resulting from the recycling of waste Residues are becoming increasingly important. An essential point this is a separation of the waste according to its size. The Separation can be done before recycling the waste become; however, it can also be an essential procedural step be in waste recycling itself.

Zur Abfallbeseitigung sind thermische Verfahren bekannt, bei denen der Abfall in Müllverbrennungsanlagen verbrannt oder in Pyrolyseanlagen pyrolisiert, d.h. unter Luftabschluß einer Temperatur von etwa 400 °C bis 700 °C unterzogen wird. Bei beiden Verfahren ist es sinnvoll, den nach der Verbrennung bzw. den nach der Pyrolyse verbleibenden Reststoff zu trennen, um ihn entweder einer Wiederverwertung zuzuführen oder ihn in geeigneter Weise zu entsorgen. Ziel ist es dabei, den auf einer Deponie endzulagernden Reststoff möglichst gering zu halten.Thermal processes are known for waste disposal, at where the waste is burned in waste incineration plants or in Pyrolysis plants pyrolyzed, i.e. in the absence of air Temperature from about 400 ° C to 700 ° C is subjected. at Both methods make sense after the combustion or to separate the residue remaining after pyrolysis, to either recycle it or dispose of it in a suitable manner. The aim is to residual material to be disposed of in a landfill as low as possible to keep.

Aus der EP-A-0 302 310 und aus der Firmenschrift "Die Schwel-Brenn-Anlage, eine Verfahrensbeschreibung", Herausgeber Siemens AG, Berlin und München, 1996, ist als Pyrolyseanlage eine sogenannte Schwel-Brenn-Anlage bekannt, bei der im wesentlichen ein zweistufiges Verfahren durchgeführt wird. In der ersten Stufe wird der angelieferte Abfall in eine Schweltrommel (Pyrolysereaktor) eingebracht und dort verschwelt (pyrolisiert). Bei der Pyrolyse entstehen in der Schweltrommel Schwelgas und Pyrolysereststoff. Das Schwelgas wird zusammen mit brennbaren Teilen des Pyrolysereststoffs in einer Hochtemperatur-Brennkammer bei Temperaturen von ca. 1200 °C verbrannt. Die dabei entstehenden Abgase werden anschließend gereinigt.From EP-A-0 302 310 and from the company publication "Die Schwel-Brenn-Anlage, a description of the process ", publisher Siemens AG, Berlin and Munich, 1996, is a pyrolysis plant so-called smoldering plant known, in which essentially a two-step process is carried out. In The first step is the delivered waste in a smoldering drum (Pyrolysis reactor) introduced and charred there (Pyrolyzed). During pyrolysis, the smoldering drum is formed Smoldering gas and pyrolysis residue. The smoldering gas becomes together with combustible parts of the pyrolysis residue in one High temperature combustion chamber at temperatures of approx. 1200 ° C burned. The resulting exhaust gases are then cleaned.

Der Pyrolysereststoff weist neben den brennbaren Teilen auch nichtbrennbare Anteile auf. Die nichtbrennbaren Anteile setzen sich im wesentlichen aus einer Inertfraktion, wie Glas, Steine oder Keramik, sowie aus einer Metallfraktion zusammen. Die Wertstoffe des Reststoffs werden aussortiert und der Wiederverwertung zugeführt. Für die Aussortierung sind Verfahren und Komponenten notwendig, die einen zuverlässigen und kontinuierlichen Betrieb gewährleisten.In addition to the combustible parts, the pyrolysis residue also has non-combustible parts. Put the non-combustible parts essentially consists of an inert fraction, such as glass, Stones or ceramics, as well as composed of a metal fraction. The recyclable materials are sorted out and recycled fed. There are procedures for sorting out and components necessary that are reliable and continuous Ensure operation.

Bei Siebvorrichtungen besteht oftmals das Problem, daß sich die Siebflächen zusetzen. Dann fällt die Siebvorrichtung aus, oder sie muß zumindest einer aufwendigen und personalintensiven Reinigung unterzogen werden. Das Problem der Verstopfung der Siebvorrichtung tritt insbesondere bei einer stark inhomogenen Zusammensetzung des zu trennenden Feststoffs auf. So verhaken sich beispielsweise Drähte in als Siebflächen verwendeten Lochblechen, so daß die einzelnen Löcher zunächst verengt werden und sich mit der Zeit zusetzen.The problem with screening devices is often that clog the sieve surfaces. Then the screening device fails, or it must at least be a complex and labor-intensive one Undergo cleaning. The problem of constipation the screening device occurs particularly in the case of a strongly inhomogeneous Composition of the solid to be separated. So for example, wires get caught in screen surfaces Perforated sheets, so that the individual holes first be narrowed and clog up over time.

Der bei der Pyrolyse anfallende Reststoff ist typischerweise ein solch stark inhomogener Feststoff, der hinsichtlich seiner stofflichen Zusammensetzung, seiner Größe und der Geometrie seiner Feststoffteile große Unterschiede aufweist. In dem Reststoff befinden sich neben Steinen, Glasscherben und größeren Metallteilen auch langgestreckte Stangen sowie in sich verwundene Drähte (Drahtgewölle).The residue obtained during pyrolysis is typical such a strongly inhomogeneous solid, which with regard to its material composition, its size and geometry its solid parts shows great differences. In the residue is next to stones, broken glass and larger metal parts also elongated bars as well as in twisted wires (wire bulges).

Zur Trennung von grobem Pyrolysereststoff ist beispielsweise aus der WO 97/26495 eine Austragsvorrichtung für Pyrolysereststoff aus einer Schweltrommel bekannt. Die Austragsvorrichtung umfaßt eine Fördereinrichtung, die einen sägezahnartig profilierten Trennboden mit einem daran angeschlossenen Stangensieb aufweist. Der Trennboden wird in Schwingungen versetzt, so daß sich auf dem Trennboden die feinen von den groben Anteilen trennen. Die feinen Anteile fallen durch das anschließende Stangensieb hindurch, während die groben Anteile auf dem Stangensieb weitergleiten. Drahtgewölle kann sich jedoch an den Stangen verhängen und zu einer Verstopfung führen.For the separation of coarse pyrolysis residue is, for example from WO 97/26495 a discharge device for pyrolysis residues known from a smoldering drum. The discharge device includes a conveyor that has a sawtooth profiled partition with an attached Rod screen has. The partition will vibrate offset so that the fine of the separate coarse parts. The fine parts fall through subsequent rod sieve through, while the coarse fractions slide on the bar screen. Wirewalls can however, hang on the poles and cause constipation to lead.

Aus der EP 0 086 488 A2 ist eine Pyrolyseanlage für Müll mit einer Siebvorrichtung für Feststoff bekannt, wobei die Siebvorrichtung um ihr Längsachse drehbar ist.EP 0 086 488 A2 also includes a pyrolysis plant for waste known a screening device for solid, the screening device is rotatable about its longitudinal axis.

Die FR 27 45 204 A1 offenbart darüber hinaus die Verwendung einer entlang einer Schraubenlinie gewundenen Stange bei einer Siebvorrichtung.FR 27 45 204 A1 also discloses the use a rod wound along a helix at one Screening device.

Der vorliegenden Erfindung liegt die Aufgabe zugrunde, eine Pyrolyseanlage für Müll mit einer Siebvorrichtung für festen Reststoff anzugeben, bei der ein kontinuierlicher Betrieb mit einfachen Mitteln gewährleistet ist, ohne daß Verstopfungen auftreten. The present invention has for its object a Pyrolysis plant for waste with a sieve for solid Specify residual material in the case of continuous operation with simple means is guaranteed without constipation occur.

Diese Aufgabe wird gemäß der Erfindung durch eine Pyrolyseanlage mit den Merkmalen des Anspruchs 1 gelöst.This object is achieved according to the invention by a pyrolysis plant solved with the features of claim 1.

Ein Vorteil einer derartig ausgestalteten Siebvorrichtung ist darin zu sehen, daß an der Stange kein Drahtgewölle oder sonstiger Feststoff haften bleiben kann. Denn durch die Drehung der Siebvorrichtung wird das Drahtgewölle aufgrund der Stangenwindung in Förderrichtung von dieser heruntergeschoben. Verstopfungen sind also wirksam vermieden.One advantage of a screening device designed in this way is to be seen in the fact that there are no piles of wire or other solid can stick. Because by the rotation the sieve device, the wire crust due to the Rod winding pushed down in the conveying direction. Blockages are thus effectively avoided.

Das Stangenelement verläuft im wesentlichen parallel zu der von der Spirale gebildeten Außenfläche bzw. parallel zu der von dem mehrgängigen Sieb gebildeten Außenfläche und wirkt folgendermaßen als Abstreifelement: Verhakt sich ein Drahtgewölle an der Stange, so wird dieses Drahtgewölle aufgrund der Drehbewegung des Siebs gegen das feststehende Stangenelement geführt und wird durch dieses entlang der Schraubenlinie von der Stange abgestreift. Um dies zu erreichen ist der Drehsinn der Stange auf die Drehrichtung der Siebvorrichtung geeignet abgestellt.The rod member is substantially parallel to that formed by the spiral outer surface or parallel to the formed by the multi-course screen and acts as a wiping element as follows: a wire bulge gets caught on the pole, this wire bulge is due to the Rotary movement of the sieve against the fixed rod element out and is guided by this along the helix of stripped the rod. To achieve this is the sense of rotation the rod to the direction of rotation of the screening device switched off.

In einer bevorzugten Ausführung ist die Stange als Spirale mit mehreren Windungen, insbesondere mit etwa vier bis zehn Windungen, ausgebildet.In a preferred embodiment, the rod is a spiral with several turns, in particular with about four to ten Turns, formed.

Bei einer derartigen Siebvorrichtung, die auch als "Spiralsieb" bezeichnet werden kann, wird der zu siebende Feststoff in den von der dreidimensionalen Spirale gebildeten Innenraum eingebracht. Feiner Feststoff, der geringere Ausmaße aufweist als der Abstand zwischen zwei Windungen der Spirale, fällt durch die Spirale hindurch, während grober Feststoff im Innenraum weiter gefördert wird. Durch eine geeignete Wahl der Abstände zwischen den Windungen kann die maximale Größe des gesiebten feineren Feststoffanteils eingestellt werden. Durch die Drehbewegung der Spirale wird ein sicherer und kontinuierlicher Transport der gröberen Feststoffteile in Förderrichtung vom Spiralbeginn zum Spiralende gewährleistet.In such a screening device, which is also called a "spiral screen" can be called the solid to be sieved into the interior formed by the three-dimensional spiral brought in. Fine solid with smaller dimensions as the distance between two turns of the spiral falls through the spiral while coarse solid in the interior is further promoted. By an appropriate choice of Spacing between turns can be the maximum size of the sieved finer solids content can be adjusted. By the rotation of the spiral becomes more secure and continuous Transport of the coarser solid parts in the conveying direction guaranteed from the beginning of the spiral to the end of the spiral.

Ein wesentlicher Vorteil bei der Spirale besteht darin, daß eventuell zwischen zwei Windungen festgeklemmte Abfallteile durch die Drehbewegung emporgehoben werden und insbesondere am oberen Umkehrpunkt aufgrund ihres Eigengewichts herabfallen. Die einfache und robuste Ausgestaltung der Siebvorrichtung als Spirale vermeidet daher selbsttätig bleibende Verstopfungen und ermöglicht einen kontinuierlichen Betrieb.A major advantage of the spiral is that any waste parts stuck between two turns be lifted up by the rotary movement and in particular fall at the upper turning point due to their own weight. The simple and robust design of the screening device as a spiral, therefore, avoids permanent constipation and enables continuous operation.

In einer zweckdienlichen Ausführung ist eine Anzahl von Stangen vorgesehen, deren Stangenanfänge drehversetzt angeordnet sind. Jede Stange verläuft dabei entlang einer Schraubenlinie. Ein solches Sieb mit mehreren Stangen wird auch als mehrgängiges Sieb bezeichnet.A number of rods are in a practical embodiment provided, the rod beginnings arranged rotatably are. Each bar runs along a helix. Such a sieve with several rods is also called multi-pass sieve.

In einer zu dem Spiralsieb alternativen Ausführungsform ist der Drehwinkel der Stangen kleiner als 360°. Insbesondere ist der Drehwinkel kleiner oder etwa gleich 180°. Durch die Ausgestaltung mit mehreren Stangen, die keine volle Umdrehung vollziehen, kann die Siebvorrichtung im Vergleich zu einem Spiralsieb mit mehreren Windungen robuster ausgestaltet werden.In an alternative embodiment to the spiral screen the angle of rotation of the rods is less than 360 °. In particular is the angle of rotation is less than or approximately equal to 180 °. By design with multiple rods that are not a full turn can perform the screening device compared to one Spiral sieve with several turns can be made more robust.

Für ein möglichst effizientes Abstreifen ist das Stangenelement bevorzugt ebenfalls entlang einer Schraubenlinie gewunden, und zwar insbesondere gegenläufig zu der Stange, so daß es mit der Stange beispielsweise einen Winkel von bevorzugt 90° einschließt.The rod element is for the most efficient stripping preferably also wound along a helix, and in particular counter to the rod, so that it with the rod, for example, an angle of preferred 90 ° includes.

In einer besonders vorteilhaften Ausgestaltung ist beim Spiralsieb die Spirale nur an einem ihrer beiden Enden befestigt, so daß die Spiralachse aufgrund des Eigengewichts zu ihrem unbefestigten Ende hin in Richtung der Schwerkraft nach unten gekrümmt ist. Bevorzugt wird die Spirale nur am Spiralbeginn gehalten, während das in Förderrichtung gelegene Spiralende frei hängend ausgebildet ist.In a particularly advantageous embodiment, the spiral screen the spiral is attached to only one of its two ends, so that the spiral axis due to its own weight towards its gravity towards its unpaved end is curved below. The spiral is preferred only at the beginning of the spiral held while the spiral end located in the conveying direction is designed to hang freely.

Alternativ zu einer einseitig befestigten Spirale kann auch eine bereits gekrümmt ausgebildete Spirale beidseitig befestigt werden. Wesentlich ist, daß die Spirale gekrümmt ist.As an alternative to a spiral fixed on one side can also an already curved spiral attached on both sides become. It is essential that the spiral is curved.

Der entscheidende Vorteil der Krümmung ist darin zu sehen, daß die Abstände der Windungen an der unteren Seite der Spirale kleiner sind als die Abstände an der Oberseite der Spirale. In die Spirale eingebrachter Feststoff kann sich prinzipiell nur zwischen Windungen auf der unteren Seite der Spirale verklemmen, da er - sobald hochgehoben - aufgrund seines Eigengewichts nach unten fällt. Mit anderen Worten: Durch die Spiralbewegung wird ein verklemmtes Feststoffteil mit der Spirale nach oben angehoben. Zugleich weitet sich der Abstand der Windungen, so daß das Feststoffteil zwischen den Windungen nicht festgeklemmt bleiben kann und aufgrund seines Eigengewichts zwangsläufig herabfällt. Die Siebvorrichtung mit gekrümmter Spirale ist somit in hohem Maße selbstreinigend.The main advantage of curvature is that that the distances of the turns at the bottom of the spiral are smaller than the distances at the top of the spiral. Solid matter introduced into the spiral can in principle only between turns on the lower side of the spiral jam because as soon as it is lifted due to its Dead weight falls down. In other words: through the Spiral movement becomes a jammed solid part with the Spiral raised up. At the same time, the distance is widening of the turns so that the solid part between the turns cannot remain clamped and due to its own weight inevitably falls down. The screening device with curved spiral is therefore highly self-cleaning.

Um die Krümmung der Spirale zu ermöglichen, ist es zweckdienlich, die Spirale flexibel auszugestalten. Zugleich werden dadurch Spannungen, die durch eingeklemmte Feststoffteile auf die Spirale einwirken, gering gehalten.In order to allow the spiral to bend, it is useful to to make the spiral flexible. At the same time this causes tensions caused by trapped solid parts act the spiral, kept low.

Für eine stabile und einfache Ausführung ist die die Spirale bildende Stange vorteilhafterweise metallisch und insbesondere ein Rundeisen oder ein Rohr aus Eisen oder Stahl. Eine solche Spirale ist äußerst robust und eignet sich insbesondere auch zur Grobtrennung von schweren und großen Feststoffen. Für Anwendungsfälle, bei denen nur geringe Belastungen auftreten, ist die Spirale beispielsweise aus Kunststoff.This is the spiral for a stable and simple design forming rod advantageously metallic and in particular a round bar or a pipe made of iron or steel. A such a spiral is extremely robust and is particularly suitable also for rough separation of heavy and large solids. For applications in which only low loads are involved occur, the spiral is made of plastic, for example.

In einer besonders bevorzugten Ausgestaltung ist zur Ausrichtung von langgestreckten Feststoffteilen in Förderrichtung bei der Siebvorrichtung eine Ausrichtvorrichtung vorgesehen, die in Förderrichtung vor der Stange angeordnet ist, und die in den Innenraum mündet.In a particularly preferred embodiment is for alignment of elongated solid parts in the conveying direction an alignment device is provided in the screening device, which is arranged in the conveying direction in front of the rod, and the flows into the interior.

Die Ausrichtung der langgestreckten Feststoffteile stellt sicher, daß diese im wesentlichen parallel zu der Längsachse in den Innenraum eingebracht werden. Langgestreckte Feststoffteile werden daher ebenfalls automatisch als grobe Feststoffteile behandelt und weiterbefördert. Sie können nicht senkrecht zur Längsachse durch die Spirale hindurch fallen. Somit ist gewährleistet, daß durch das von der Stange bzw. von den Stangen gebildete Sieb ausschließlich Feststoffteile durchfallen, deren größte Abmessung kleiner ist als der Abstand zweier Windungen der Spirale bzw. als der Abstand zweier Stangen.The alignment of the elongated solid parts ensures that this is essentially parallel to the longitudinal axis in the interior can be introduced. Elongated solid parts are therefore also automatically as coarse solid parts treated and promoted. You can't be vertical fall through the spiral to the longitudinal axis. Consequently is guaranteed that by the off the shelf or by the The sieve formed from rods only falls through solid particles, whose largest dimension is smaller than the distance two turns of the spiral or as the distance between two Rods.

Um ein einfaches Ausrichten der langgestreckten Feststoffteile zu gewährleisten, ist die Ausrichtvorrichtung als eine um ihre Längsachse drehbare Trommel ausgestaltet. Aufgrund der Drehbewegung der Trommel richten sich die Feststoffteile automatisch in Richtung der Trommelachse aus.For easy alignment of the elongated solid parts To ensure the alignment device is as one configured drum rotatable about its longitudinal axis. by virtue of the solid parts are aligned with the rotary movement of the drum automatically in the direction of the drum axis.

Besonders vorteilhaft ist die Anordnung einer Wendel an der Innenseite der Trommel, also die Anordnung einer schraubenförmig gewundenen Leiste. Mit dieser Wendel wird verhindert, daß Feststoff, der beispielsweise über einen Einfüllschacht in das eine Trommelende eingebracht wird, die Trommel mit einer zu großen Geschwindigkeit durchläuft, so daß der Feststoff durch den von der Stange gebildeten Innenraum "hindurchfliegt", ohne daß eine Siebung stattfindet. Bevorzugt ist die Wendel hierzu mehrgängig ausgebildet, d.h. es sind mehrere schraubenförmige Leisten vorgesehen, die drehversetzt angeordnet sind. Die Wendel ist insbesondere unmittelbar an der Einlaßseite der Trommel angeordnet und weist eine relativ hohe Flanke auf.The arrangement of a helix on the Inside of the drum, so the arrangement of a helical winding ledge. This spiral prevents that solid, for example, through a feed chute into which one end of the drum is inserted, the drum with a passes through at high speed so that the solid "flies" through the interior space formed by the rod, without screening. Prefers the helix is multi-start, i.e. there are several helical strips are provided, which are rotationally offset are arranged. The helix is particularly immediately on arranged on the inlet side of the drum and has a relative high flank.

Die Wendel ist insbesondere derart ausgebildet, daß sie - in einer Draufsicht in Richtung der Längsachse der Trommel gesehen - einen geschlossenen Kreis bildet. Damit ist ausgeschlossen, daß Feststoff am Trommelboden geradlinig vom Trommeleingang bis zum Trommelausgang ohne Hindernis hindurchgleiten kann. Um den Feststoffluß nicht unnötig zu behindern, wird eine mehrgängige Wendel mit einem Drehwinkel kleiner 360° bevorzugt. In diesem Fall wird der gewünschte Überlapp der Flanke erreicht und gleichzeitig wird eine relativ flache Steigung der Wendel ermöglicht, so daß ein schneller Feststofftransport innerhalb der Trommel ermöglicht ist.The helix is in particular designed such that it - in a plan view seen in the direction of the longitudinal axis of the drum - forms a closed circle. This means that that solids on the drum bottom straight from the drum entrance slide through to the drum exit without any obstacles can. In order not to obstruct the flow of solids unnecessarily, becomes a multi-turn helix with an angle of rotation smaller 360 ° preferred. In this case, the desired overlap the flank reaches and at the same time becomes a relatively flat one Incline of the helix allows for a faster solids transport inside the drum.

In einer alternativen Ausgestaltung ist die Ausrichtvorrichtung als ein mit Längsrillen versehener profilierter Schwingboden ausgestaltet, bei dem die Längsrillen in Förderrichtung verlaufen und bei dem die langgestreckten Feststoffteile aufgrund der Schwingungen des Schwingbodens in diesen Längsrillen ausgerichtet werden.In an alternative embodiment, the alignment device as a profiled oscillating floor with longitudinal grooves designed in which the longitudinal grooves in the conveying direction run and in which the elongated solid parts due the vibrations of the vibrating floor in these longitudinal grooves be aligned.

Die Stange ist vorteilhafterweise an der in Förderrichtung gelegenen Stirnseite der Trommel an dieser befestigt und dort insbesondere verschweißt. Die Stange ist bevorzugt derart befestigt, daß der Trommelausgang in den von der Stange gebildeten Innenraum mündet. Für einen reibungslosen Materialaustrag aus der Trommel ist die Stange also auf der Trommelaußenwand oder zumindest mit der Trommel fluchtend befestigt.The rod is advantageously on the in the conveying direction end face of the drum attached to this and there especially welded. The rod is preferably attached in such a way that the drum exit in the formed by the rod Interior opens. For a smooth material discharge the rod is out of the drum on the outer wall of the drum or at least attached flush with the drum.

Bei dieser konstruktiven Ausgestaltung bilden Ausrichtvorrichtung und Stange eine besonders einfach ausgestaltete Baueinheit, die robust und zuverlässig ist.In this constructive configuration form alignment device and rod a particularly simple construction unit, that is robust and reliable.

Die Siebvorrichtung ist in einer besonders bevorzugten Ausführungsform mit der Austragsseite der Schweltrommel der Pyrolyseanlage zur Siebung von aus der Schweltrommel erhaltenen Pyrolysereststoffen verbunden.The screening device is in a particularly preferred embodiment with the discharge side of the smoldering drum of the pyrolysis plant for screening of those obtained from the smoldering drum Pyrolysis residues connected.

Mit der Siebvorrichtung wird bei der Pyrolyseanlage bevorzugt eine erste Trennung des Pyrolysereststoffs in eine feine und eine grobe Reststoffraktion vorgenommen. Aufgrund der einfachen und besonders robusten Ausgestaltung der Siebvorrichtung ist ein sicherer und kontinuierlicher Betrieb der gesamten Pyrolyseanlage sichergestellt.With the sieve device is preferred in the pyrolysis plant a first separation of the pyrolysis residue into a fine and made a rough residue fraction. Because of the simple and particularly robust design of the screening device is a safe and continuous operation of the whole Pyrolysis plant ensured.

Besonders vorteilhaft und zweckdienlich ist es, die Siebvorrichtung unmittelbar mit der Schweltrommel an deren Austragsseite fest zu verbinden. Somit sind zwischen der Schweltrommel und der Siebvorrichtung keine weiteren Komponenten zwischengeschaltet, die eine Störung verursachen können. Die Stange ist beispielsweise unmittelbar an einem Austragsrohr der Schweltrommel befestigt und innerhalb einer Austragsvorrichtung angeordnet. Diese Austragsvorrichtung ist bevorzugt gegen die Außenatmosphäre gasdicht abgedichtet, um den Eintritt von Luftsauerstoff zu vermeiden, der zu einer Verbrennung des brennbaren und heißen Pyrolysereststoffs führen würde.It is particularly advantageous and expedient to use the screening device directly with the smoldering drum on the discharge side to connect firmly. So are between the smoldering drum and no further components are interposed between the screening device, that can cause interference. The Rod is, for example, directly on a discharge pipe attached to the smoldering drum and within a discharge device arranged. This discharge device is preferred sealed gas-tight from the outside atmosphere to prevent entry to avoid atmospheric oxygen leading to combustion of the combustible and hot pyrolysis residue.

Insbesondere zum Zweck der Grobsiebung von Reststoff aus einer großtechnischen Pyrolyseanlage beträgt der Abstand zwischen zwei Windungen der Spirale bzw. zwischen zwei Stangen vorteilhafterweise etwa 100 mm bis 300 mm und insbesondere etwa 180 mm. Der von der Stange gebildete Innenraum weist eine Länge von etwa 0,5 bis 1,5 m auf. Sein Durchmesser beträgt etwa 1,5 m, und eine Siebvorrichtung mit Trommel und Sieb weist bevorzugt eine Gesamtlänge von etwa 2 bis 4 m auf. Die Länge des Innenraums ist zweckmäßigerweise kleiner oder gleich dem Durchmesser der Trommel.In particular for the purpose of coarse screening of residual material from a industrial pyrolysis plant is the distance between two turns of the spiral or between two rods advantageously about 100 mm to 300 mm and in particular about 180 mm. The interior formed by the rod has one Length of about 0.5 to 1.5 m. Its diameter is about 1.5 m, and a sieve device with drum and sieve preferably has a total length of about 2 to 4 m. The Length of the interior is suitably less or equal to the diameter of the drum.

Im folgenden wird die Erfindung und vorteilhafte Ausgestaltungen anhand der Zeichnung näher erläutert. Es zeigen jeweils in einer schematischen Ansicht:

FIG 1
eine Siebvorrichtung, bei der eine Trommel als Ausrichtvorrichtung mit einer Spirale fest verbunden ist,
FIG 2
einen Schnitt durch eine gekrümmte Spirale zur Erläuterung der vorteilhaften Wirkung der Siebvorrichtung,
FIG 3
eine Schweltrommel mit daran befestigter Spirale, und
FIG 4
eine Siebvorrichtung mit einer Anzahl von Stangen als mehrgängiges Sieb.
The invention and advantageous embodiments are explained in more detail below with reference to the drawing. Each shows in a schematic view:
FIG. 1
a screening device in which a drum is firmly connected as an alignment device with a spiral,
FIG 2
2 shows a section through a curved spiral to explain the advantageous effect of the screening device,
FIG 3
a smoldering drum with attached spiral, and
FIG 4
a sieve device with a number of rods as a multi-start sieve.

Gemäß Figur 1 umfaßt eine Siebvorrichtung 1 eine Ausrichtvorrichtung, und zwar eine um ihre Längsachse drehbare Trommel 2, die gegenüber der Horizontalen geneigt ist. An deren linken Stirnseite 4 ist eine schaftartige Aufgabevorrichtung 6 für Feststoff R angeordnet. Bei diesem Feststoff R handelt es sich z.B. um Pyrolysereststoff oder Bauschutt. An der der Aufgabevorrichtung 6 gegenüberliegenden rechten Stirnseite 7 der Trommel 2 ist eine entlang einer Schraubenlinie gewickelte Stange 8 aus Metall befestigt, die eine Spirale 10 mit einem Innenraum 11 bildet. Die Spirale 10 ist beispielsweise mit einer geeigneten Schweiß-, Schraub- oder Klemmverbindung an der Trommel 2 befestigt. Die Spirale 10 fluchtet in etwa mit der Trommel 2, so daß der Durchmesser der Trommel 2 und der der Spirale 10 etwa gleich sind. Dies ermöglicht, daß die gesamte rechte Stirnseite 7 als Trommelausgang für den Feststoff R verwendet werden kann, und daß die Trommel 2 beispielsweise als einfaches Rohr aus Metall ausgestaltet sein kann. Die gemeinsame Längsachse 3 der Siebvorrichtung 1 und der Trommel 2 fällt im wesentlichen mit der Spiralachse 12 der Spirale 10 zusammen.According to FIG. 1, a screening device 1 comprises an alignment device, namely a drum rotatable about its longitudinal axis 2, which is inclined to the horizontal. On theirs left end face 4 is a shaft-like feeder 6 arranged for solid R. With this solid R e.g. pyrolysis residue or rubble. On the right of the feeder 6 opposite Front 7 of drum 2 is one along a helix coiled rod 8 made of metal attached to a spiral 10 with an interior 11 forms. The spiral 10 is for example with a suitable welding, screwing or Clamp connection attached to the drum 2. The spiral 10 aligns approximately with the drum 2, so that the diameter the drum 2 and that of the spiral 10 are approximately the same. This allows the entire right face 7 as a drum exit can be used for the solid R, and that the drum 2, for example, as a simple tube made of metal can be designed. The common longitudinal axis 3 of the screening device 1 and the drum 2 essentially falls with the Spiral axis 12 of the spiral 10 together.

Die Trommel 2 ist drehbar gelagert. Sie kann über einen nicht näher dargestellten Antrieb in Rotation versetzt werden. Zusammen mit der Trommel 2 rotiert auch die an der Trommel 2 befestigte Spirale 10. Diese weist gemäß Figur 1 fünf Windungen auf. Der Abstand zwischen zwei benachbarten Windungen richtet sich nach der Art des Feststoffs R. Er beträgt vorliegend vorzugsweise etwa 180 mm. Die spiralförmig gewickelte Stange 8 besteht aus einem robusten Material und ist insbesondere metallisch. Sie ist beispielsweise ein Rundeisen oder ein Stahlrohr. Die Spirale 10 ist nur einseitig, und zwar an der Trommel 2, befestigt. Ihr der Trommel 2 abgewandtes Spiralende ist frei von Befestigungsmitteln und wird nicht abgestützt. Die Spirale 10 wird sich daher zu ihrem unbefestigten Ende hin aufgrund der Schwerkraft nach unten krümmen. Hierauf wird weiter unten zur Figur 2 näher eingegangen.The drum 2 is rotatably supported. You can't over one drive shown in detail can be set in rotation. Together the drum 2 also rotates the drum 2 attached spiral 10. This has five turns according to Figure 1 on. The distance between two adjacent turns depends on the type of solid R. It is present preferably about 180 mm. The spiral wound Rod 8 is made of a robust material and is special metallic. For example, it is a round bar or a steel pipe. The spiral 10 is only one-sided, namely on the drum 2 attached. Your spiral end facing away from drum 2 is free of fasteners and is not supported. The spiral 10 will therefore become unpaved Bend downward due to gravity. hereupon is discussed in more detail below in FIG. 2.

Der Feststoff R wird über die Aufgabevorrichtung 6 in die Trommel 2 gegeben und wird aufgrund der Neigung der Trommel 2 und der Drehbewegung in Förderrichtung 14 zur Spirale 10 hin transportiert. In der Spirale 10 wird feiner Feststoff F abgetrennt, während grober Feststoff G von der Spirale 10 weitertransportiert wird.The solid R is the feed device 6 in the Drum 2 is given and is due to the inclination of the drum 2nd and the rotational movement in the conveying direction 14 towards the spiral 10 transported. Fine solid F is separated off in the spiral 10, while coarse solid G is transported further by the spiral 10 becomes.

Ein wesentlicher Vorteil der Siebvorrichtung 1 mit der Spirale 10 ist darin zu sehen, daß selbst schwer fließender Feststoff R durch die Drehbewegung in einfacher Weise in Förderrichtung 14 transportiert wird.A major advantage of the screening device 1 with the spiral 10 can be seen in the fact that even more fluent Solid R through the rotary movement in a simple manner in the conveying direction 14 is transported.

Aufgrund der Drehbewegung der Trommel 2 richten sich zugleich langgestreckte Feststoffteile 16 in Förderrichtung 14 aus, so daß sie etwa parallel zur Spiralachse 12 in den Innenraum 11 der Spirale 10 geführt werden. Dadurch wird sicher vermieden, daß die langgestreckten Feststoffteile 16 senkrecht zur Spiralachse 12 in die Spirale 10 gelangen und durch die Spirale 10 durchfallen. Durch die Spirale 10 kann daher nur der feine Feststoff F hindurchfallen, der in einem ersten Sammelbehälter 18 gesammelt und bei Bedarf abtransportiert wird. Der grobe Feststoff G wird durch die Spirale 10 hindurchgeführt. Er fällt am Ende der Spirale 10 in einen zweiten Sammelbehälter 20 und wird ebenfalls bei Bedarf abtransportiert. Anstelle der Sammelbehälter 18, 20 können auch Fördervorrichtungen, wie Transportbänder oder Transportschnecken, vorgesehen sein, um den Feststoff F, G kontinuierlich abzutransportieren.Due to the rotary movement of the drum 2 align at the same time elongated solid parts 16 in the conveying direction 14, so that they are approximately parallel to the spiral axis 12 in the interior 11th the spiral 10 are guided. This will surely avoid that the elongated solid parts 16 perpendicular to the spiral axis 12 get into the spiral 10 and through the spiral 10 fail. Due to the spiral 10, only the fine solid F fall through it in a first collection container 18 collected and transported if necessary. The coarse solid G is passed through the spiral 10. At the end of the spiral 10, it falls into a second collecting container 20 and will also be removed if necessary. Instead of the collecting containers 18, 20, conveying devices, such as conveyor belts or screw conveyors be to continuously remove the solid F, G.

Figur 2 zeigt einen schematischen Schnitt durch eine gekrümmte Spirale 10. Hieran wird das wesentliche Funktionsprinzip der gekrümmten Spirale 10 erläutert. Die Spiralachse 12 (und mit ihr die gesamte Spirale 10) weist gemäß Figur 2 eine Krümmung auf. Aufgrund der Krümmung ist der obere Abstand o zwischen zwei aufeinanderfolgenden Windungen größer als der untere Abstand u zwischen zwei Windungen. Ein Feststoffteil R kann sich nur im unteren Bereich der Spirale 10 festklemmen, wo der Abstand u zwischen zwei Windungen klein ist. Ein festgeklemmtes Feststoffteil P wird durch die Drehbewegung der Spirale 10 nach oben gefördert, und gleichzeitig wird der Abstand der Windungen größer, so daß sich das Feststoffteil P löst und herunterfällt.Figure 2 shows a schematic section through a curved Spiral 10. This is the main principle of operation of the curved spiral 10 explained. The spiral axis 12 (and with it the entire spiral 10) points according to Figure 2 shows a curvature. Because of the curvature is the top one Distance o between two successive turns larger than the lower distance u between two turns. On Solid part R can only be in the lower part of the spiral 10 clamp where the distance u between two turns is small. A clamped solid part P is through the Rotational movement of the spiral 10 promoted upward, and at the same time the distance between the turns becomes larger, so that the Solid part P loosens and falls.

Gleiches gilt in ähnlicher Weise für Drahtstücke 24 oder ähnliche Feststoffteile, die hakenförmig ausgebildet sind und sich mit der Hakenöffnung über die Stange 8 hängen. Bei einem nur in einer Ebene sich bewegenden Sieb würden solche Drahtstücke 24 in der Regel zu einer Verstopfung führen. Im vorliegenden Fall wird das Drahtstück 24 bei der Rotation zusammen mit der Spirale 10 nach oben geführt. Insbesondere am oberen Umkehrpunkt der Spirale 10 ist die Hakenöffnung nach oben gerichtet, so daß das Drahtstück 24 herunterfallen kann. Dieser vorteilhafte Mechanismus der Spirale 10 ist unabhängig davon, ob eine Krümmung der Spirale 10 vorhanden ist.The same applies in a similar way to wire pieces 24 or the like Solid parts that are hook-shaped and hang over the rod 8 with the hook opening. At a such wire pieces would only move in one plane 24 usually lead to constipation. In the present Fall, the piece of wire 24 is rotated together with the spiral 10 upwards. Especially at the top The turning point of the spiral 10 is the hook opening after directed upwards so that the wire piece 24 can fall down. This advantageous mechanism of the spiral 10 is independent whether there is a curvature of the spiral 10.

Gemäß Figur 3 wird die Schweltrommel 26 einer Pyrolyseanlage über einen Aufgabeschacht 27 und eine Zufuhreinrichtung 28 mit Abfall A beschickt. Der Abfall A wird in der Schweltrommel 26 bei etwa 450 °C verschwelt. Dabei entstehen ein Schwelgas S sowie ein Feststoff oder Pyrolysereststoff R. Die Schweltrommel 26 wird bevorzugt über nicht näher dargestellte innenliegende Heizrohre beheizt. Sie ist gegenüber der Horizontalen geneigt und drehbar gelagert. Auf der der Zufuhreinrichtung 28 gegenüberliegenden Stirnseite der Schweltrommel 26 ist ein Austragsrohr 29 angeordnet, an dem endseitig die Spirale 10 befestigt ist. Das Austragsrohr 29 und die Spirale 10 bilden die Siebvorrichtung 1. Das Austragsrohr 29 dient gleichzeitig als Ausrichtvorrichtung für langgestreckte Feststoffteile. Mit der Spirale 10 werden die feinen Feststoffanteile F von den groben Feststoffanteilen G getrennt.According to Figure 3, the smoldering drum 26 of a pyrolysis plant via a feed shaft 27 and a feed device 28 loaded with waste A. The waste A is in the smoldering drum 26 at around 450 ° C. This creates a Smoldering gas S and a solid or pyrolysis residue R. Die Smoldering drum 26 is preferred over not shown internal heating pipes heated. It is opposite the horizontal inclined and rotatable. On the feeder 28 opposite end of the smoldering drum 26, a discharge pipe 29 is arranged on the end the spiral 10 is attached. The discharge pipe 29 and the Spiral 10 form the sieve device 1. The discharge pipe 29 also serves as an alignment device for elongated Solid parts. With the spiral 10, the fine solids F separated from the coarse solids content G.

Das Austragsrohr 29 mit angeschlossener Spirale 10 mündet in einer Austragsvorrichtung 30, die gegenüber der rotierenden Schweltrommel 26 über Gleitringdichtungen 32 gasdicht abgedichtet ist. Ebenso wie die Austragsvorrichtung 30 ist auch die Zufuhreinrichtung 28 zur Schweltrommel 26 hin über Gleitringdichtungen 32 gasdicht abgedichtet. Damit soll vermieden werden, daß Luftsauerstoff in die Schweltrommel 26 eindringt und den in der Schweltrommel 26 weitgehend sauerstofffrei ablaufenden Pyrolyseprozeß beeinträchtigt. Neben dem Pyrolysereststoff R entsteht in der Schweltrommel 26 das Schwelgas S, welches über das Austragsrohr 29 in die Austragsvorrichtung 30 strömt und von dort über einen Schwelgasabzugsstutzen 34 abgeleitet wird.The discharge pipe 29 with a connected spiral 10 opens into a discharge device 30 which is opposite the rotating Smoldering drum 26 sealed gas-tight via mechanical seals 32 is. The same as the discharge device 30 the feed device 28 to the smoldering drum 26 via mechanical seals 32 sealed gas-tight. This is to be avoided be that atmospheric oxygen penetrates into the smoldering drum 26 and the one that runs largely oxygen-free in the smoldering drum 26 Pyrolysis process affected. In addition to the pyrolysis residue R arises in the carbonization drum 26, the carbonization gas S, which via the discharge pipe 29 into the discharge device 30 flows and from there via a carbonization gas outlet 34 is derived.

An die in der Austragsvorrichtung 30 angeordnete Spirale 10 kann sich in einer alternativen Ausführung ein in Figur 3 gestrichelt dargestelltes Rohr 37 anschließen, durch das der grobe Feststoff G aus der Austragsvorrichtung 30 ausgetragen wird. Die Spirale 10 ist in diesem Fall zwischen dem Austragsrohr 29 und dem Rohr 37 angeordnet.To the spiral 10 arranged in the discharge device 30 can be dashed in an alternative embodiment in Figure 3 Connect shown tube 37 through which the coarse solid G discharged from the discharge device 30 becomes. The spiral 10 is in this case between the discharge pipe 29 and the tube 37 arranged.

Mit der Anordnung der Spirale 10 am Austragsrohr 29 der Schweltrommel 26 wird der Pyrolysereststoff R unmittelbar nach der Schweltrommel 26 in einen feinen Feststoffanteil F und einen groben Feststoffanteil G getrennt. Die Gefahr einer Verstopfung von der Schweltrommel 26 nachgeschalteten Komponenten ist daher nur gering. With the arrangement of the spiral 10 on the discharge tube 29 Smoldering drum 26 is the pyrolysis residue R immediately after the smoldering drum 26 into a fine solid fraction F and a coarse solid content G separated. The danger of one Blockage from the smoldering drum 26 downstream components is therefore only minor.

Die Siebvorrichtung eignet sich generell zum direkten Anschluß an Drehrohre, wie z.B. Drehrohröfen oder Schweltrommeln, in denen der Feststoff einer Behandlung unterzogen wird, wonach er getrennt werden soll.The screening device is generally suitable for direct connection on rotating pipes, e.g. Rotary kilns or smoldering drums, in which the solid is subjected to treatment what it should be separated after.

Der mit der Siebvorrichtung 1 abgetrennte feine Reststoff F wird zur weiteren Aufbereitung vorzugsweise einer sogenannten Windsichtung unterzogen. Dabei werden die leichten, insbesondere kohlenstoffhaltigen, Feststoffanteile von den schweren Feststoffanteilen getrennt. Bei einer solchen Windsichtung wird der Feststoff einem Luftstrom zugeführt, so daß die leichten Feststoffanteile mit dem Luftstrom mitgerissen werden. Als besonders zweckdienlich hat sich ein zick-zack-förmiger Schacht herausgestellt, in den die Luft von unten und der Feststoff von oben oder seitlich zugeführt wird.The fine residual material F separated with the screening device 1 is preferably a so-called for further processing Subjected to wind sifting. The light ones, in particular carbonaceous, solids from the heavy Solid components separated. With such a wind sighting the solid is fed to an air stream so that the light solids are entrained with the air flow. A zigzag-shaped one has proven particularly useful Exposed in the air from below and shaft the solid is fed from above or from the side.

In Figur 4 ist eine zu der Spirale 10 alternative Ausführungsform dargestellt, bei der anstelle der Spirale 10 eine Anzahl von Stangen 8 am Ende der Trommel 2 angeordnet ist. Die Stangen 8 sind jeweils entlang einer Schraubenlinie gewunden und können daher als eine mehrgängige Wendel angesehen werden. Die einzelnen Stangen 8 sind zueinander am Ende der Trommel 2 bevorzugt um einen Winkel von 30° drehversetzt angeordnet. Jede einzelne Stange 8 besitzt einen Drehwinkel kleiner 360°, bildet also keine vollständige Drehung. Damit wird eine besonders robuste Ausgestaltung ermöglicht. Der entscheidende Vorteil bei dieser mehrgängigen Wendel, wie auch bei der Spirale 10 gemäß Figur 1, besteht in der Anordnung einer oder mehrerer schraubenförmig gewundener Stangen 8, so daß durch die Drehbewegung der Siebvorrichtung 1 eventuell festhängende Feststoffteile automatisch an das Ende der Siebvorrichtung weiter transportiert werden und dort abgeworfen werden.FIG. 4 shows an alternative embodiment to the spiral 10 shown, in which a instead of the spiral 10 Number of rods 8 is arranged at the end of the drum 2. The rods 8 are each wound along a helix and can therefore be regarded as a multi-start spiral become. The individual rods 8 are at the end of each other Drum 2 preferably arranged rotatably offset by an angle of 30 °. Each individual rod 8 has an angle of rotation less than 360 °, does not form a complete rotation. In order to a particularly robust design is made possible. The decisive advantage with this multi-start helix, like also with the spiral 10 according to FIG. 1, there is the arrangement one or more helically wound rods 8, so that the rotary movement of the screening device 1 any stuck solid parts automatically to the end the screening device are transported further and dropped there become.

Um diesen selbstreinigenden Mechanismus zu unterstützen ist die Anordnung eines Stangenelements 35 vorgesehen, das weitgehend parallel zu der von den Stangen 8 gebildeten Außenfläche verläuft. Das Stangenelement 35 ist ebenso bei der Ausführungsform mit der Spirale 10 angeordnet, wenn auch dort nicht im Detail gezeigt. Es bewirkt, daß ein an einer Stange 8 hängendes Feststoffteil aufgrund der Relativbewegung zwischen Stange 8 und Stangenelement 35 in Förderrichtung 14 von der Stange 8 abgezogen wird. Hierzu ist die Drehrichtung der Siebvorrichtung 1 und der Drehsinn der Stangen 8 aufeinander abgestimmt.To support this self-cleaning mechanism the arrangement of a rod member 35 provided that largely parallel to the outer surface formed by the rods 8 runs. The rod member 35 is also in the embodiment arranged with the spiral 10, although there not shown in detail. It causes one on a pole 8 hanging solid part due to the relative movement between rod 8 and rod element 35 in conveying direction 14 is withdrawn from the rod 8. This is the direction of rotation the screening device 1 and the direction of rotation of the rods 8 on top of each other Voted.

Um die Abstreifwirkung zu erhöhen, ist das Stangenelement 35 ebenfalls entlang einer Schraubenlinie gewunden und kreuzt die Stangen 8 bevorzugt unter einem Winkel von 90°. Die Steigung des Stangenelements 35 nimmt in Förderrichtung 14 bevorzugt zu, um die Abstreifwirkung zu erhöhen. Die Wirkung wird weiter verbessert, wenn mehrere Stangenelemente 35 vorgesehen sind. Beispielsweise sind diese etwa halbkreisförmig unterhalb der Stangen 8 angeordnet.In order to increase the stripping effect, the rod element 35 also wound and crossed along a helix the rods 8 preferably at an angle of 90 °. The slope of the rod element 35 preferably takes in the conveying direction 14 to increase the wiping effect. The effect will be further improved if several rod elements 35 are provided are. For example, these are approximately semicircular below the rods 8 arranged.

Ein weiterer Vorteil der Anordnung des Stangenelements 35 ist darin zu sehen, daß längliche Feststoffteile 16, die in der Trommel 2 nicht vollständig parallel zu der Längsrichtung 3 ausgerichtet werden, nicht durch einen Spalt zwischen den Stangen 8 hindurchfallen können. Aufgrund der Drehbewegung der Trommel 2 kann es nämlich vorkommen, daß die länglichen Feststoffteile 16 mit emporgehoben werden, so daß sie am Austritt der Trommel 2 unter einem spitzen Winkel auf die Stangen 8 treffen.
Aus Figur 4 ist weiterhin zu entnehmen, daß an der Einlaufseite der Trommel 2 eine mehrgängige Wendel 36 angeordnet ist. Im Ausführungsbeispiel umfaßt die mehrgängige Wendel 36 zwei schraubenlinienförmige Bleche, die zueinander drehversetzt angeordnet sind. Es können auch weitere Bleche vorgesehen sein. Die Wendel 36 ist an der Innenseite der Trommel 2 angeordnet und ist derart ausgestaltet, daß sich an jeder Stelle des Trommelbodens zumindest zwei Wendelabschnitte überlappen. Zudem sind die Flanken der Wendel, also die Bleche, relativ hoch. Damit ist sichergestellt, daß der durch die Aufgabevorrichtung 6 eingebrachte Feststoff R abgebremst wird und nicht durch die Siebvorrichtung 1 hindurchfliegt oder hindurchschießt, ohne daß der Feststoff R eine Siebung erfährt.
Another advantage of the arrangement of the rod element 35 can be seen in the fact that elongate solid parts 16, which are not aligned completely parallel to the longitudinal direction 3 in the drum 2, cannot fall through a gap between the rods 8. Because of the rotary movement of the drum 2, it may happen that the elongated solid parts 16 are also lifted up so that they meet the rods 8 at an acute angle at the outlet of the drum 2.
It can also be seen from FIG. 4 that a multi-start spiral 36 is arranged on the inlet side of the drum 2. In the exemplary embodiment, the multi-turn helix 36 comprises two helical sheets which are arranged so as to be rotationally offset from one another. Further sheets can also be provided. The coil 36 is arranged on the inside of the drum 2 and is designed in such a way that at least two coil sections overlap at each point on the drum base. In addition, the flanks of the helix, i.e. the sheets, are relatively high. This ensures that the solid R introduced by the feed device 6 is braked and does not fly through or shoot through the screening device 1 without the solid R undergoing screening.

Das zu Figur 4 beschriebene mehrgängige Sieb mit mehreren Stangen 8 kann ohne Einschränkung das Spiralsieb 10 aus Figur 3 ersetzen.The multi-pass sieve with several described for FIG Rods 8 can, without limitation, the spiral sieve 10 from FIG 3 replace.

Eine erfindungsgemäße Pyrolyseanlage mit einer Siebvorrichtung zeichnet sich durch eine sehr einfache und robuste Konstruktion aus und gewährleistet gleichzeitig einen störungsfreien Betrieb, ohne daß Verstopfungen auftreten. Entscheidende Aspekte für die Gewährleistung des sicheren Betriebs sind die Ausgestaltung der Siebvorrichtung mit der schraubenförmig gewundenen Stange 8 bzw. mit den Stangen 8, die durch die Krümmung der Spirale 10 bedingten Unterschiede im Abstand der Windungen, die sichere Abscheidung von langgestreckten Feststoffteilen aufgrund der vorgeschalteten Ausrichtvorrichtung sowie der durch die Rotationsbewegung und Spiralbewegung bedingte automatische Transport des Feststoffs R.A pyrolysis plant according to the invention with a screening device is characterized by a very simple and robust construction while ensuring trouble-free Operation without clogging. decisive Aspects for ensuring safe operation are the design of the screening device with the helical coiled rod 8 or with the rods 8 passing through the curvature of the spiral 10 caused differences in distance of the turns, the safe separation of elongated Solid parts due to the upstream alignment device as well as that by the rotational movement and spiral movement conditional automatic transport of solid R.

Claims (18)

  1. Pyrolysis plant for refuse having a screening device (1) for solid residues (R), which is rotatable about its longitudinal axis (3) and into the interior of which the residues can be introduced, characterized in that the screening device (1) has a rod (8) which is wound along a helical line and a rod element (35) is provided, which is arranged fixedly with respect to the wound rod (8) and essentially parallel to the outer face formed by the wound rod (8).
  2. Pyrolysis plant for refuse having a screening device (1) for solid residues (R) according to Claim 1, characterized in that the rod (8) is designed as a spiral (10) with a plurality of turns, in particular with about 4 to 10 turns.
  3. Pyrolysis plant for refuse having a screening device (1) for solid residues (R) according to Claim 1 or 2, characterized in that a number of rods (8) are provided, the rod starts of which are arranged so as to be offset in terms of rotation.
  4. Pyrolysis plant for refuse having a screening device (1) for solid residues (R) according to Claim 3, characterized in that the rods (8) have an angle of rotation smaller than 360°, in particular smaller than or approximately equal to 180°.
  5. Pyrolysis plant for refuse having a screening device (1) for solid residues (R) according to one of Claims 1 to 4, characterized in that the rod element (35) is wound along a helical line in opposition to the rod (8), so that the said rod element forms, in particular, an angle of about 90° with the rod (8).
  6. Pyrolysis plant for refuse having a screening device (1) for solid residues (R) according to one of Claims 1 to 5, characterized in that a plurality of rod elements (35) are provided, the starts of which are arranged so as to be offset in terms of rotation.
  7. Pyrolysis plant for refuse having a screening device (1) for solid residues (R) according to one of Claims 1 to 6, characterized in that the rod (8) is fastened only at its rod start.
  8. Pyrolysis plant for refuse having a screening device (1) for solid residues (R) according to one of Claims 1 to 7, characterized in that the rod (8) is flexible.
  9. Pyrolysis plant for refuse having a screening device (1) for solid residues (R) according to one of Claims 2 to 8, characterized in that the spiral axis (12) of the spiral (10) is curved downwards.
  10. Pyrolysis plant for refuse having a screening device (1) for solid residues (R) according to one of Claims 1 to 9, characterized in that the rod (8) is metallic and, in particular, is a round iron bar or a tube.
  11. Pyrolysis plant for refuse having a screening device (1) for solid residues (R) according to one of Claims 1 to 10, characterized in that an aligning device is provided for the alignment of elongate solid fragments in the conveying direction (14), the said aligning device being arranged upstream of the rod (8) and opening into the interior (11).
  12. Pyrolysis plant for refuse having a screening device (1) for solid residues (R) according to Claim 11, characterized in that the aligning device is a drum (2) rotatable about its longitudinal axis (3).
  13. Pyrolysis plant for refuse having a screening device (1) for solid residues (R) according to Claim 12, characterized in that the rod (8) is fastened, in particular welded, to the drum (2) on the end face (4) located in the conveying direction (14).
  14. Pyrolysis plant for refuse having a screening device (1) for solid residues (R) according to Claim 12 or 13, characterized in that a coil (36), preferably a multi-flight coil (36), is arranged on the inside of the drum (2).
  15. Pyrolysis plant for refuse having a screening device (1) for solid residues (R) according to Claim 14, characterized in that the coil (36) is designed in such a way that it forms a closed circle, as seen in a top view in the direction of the longitudinal axis (3) of the drum (2).
  16. Pyrolysis plant for refuse having a screening device (1) for solid residues (R) according to one of Claims 1 to 15, characterized in that the screening device (1) is connected to a discharge side of a low-temperature carbonization drum (26) for the screening of pyrolysis residues obtained from the low-temperature carbonization drum (26).
  17. Pyrolysis plant for refuse having a screening device (1) for solid residues (R) according to one of Claims 1 to 16, characterized in that the distance between two turns of the spiral (10) or between two rods (8) is about 100 to 300 mm, in particular 180 mm.
  18. Pyrolysis plant for refuse having a screening device (1) for solid residues (R) according to one of Claims 1 to 17, characterized in that the interior (11) formed by the rod (8) has a diameter of about 1.5 m and a length of about 0.5 to 1.5 m.
EP99936263A 1998-05-22 1999-05-17 Sieving device for solid material and a method for sieving solid material Expired - Lifetime EP1144137B1 (en)

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EP03011845A EP1348492B1 (en) 1998-05-22 1999-05-17 Pyrolysis plant for waste with screening device for residual solids
DK03011845T DK1348492T3 (en) 1998-05-22 1999-05-17 Pyrolysis plant for waste and with a solid residue soldering device

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DE19823018 1998-05-22
DE19823018A DE19823018A1 (en) 1998-05-22 1998-05-22 Solid material screening device
PCT/DE1999/001482 WO1999061172A2 (en) 1998-05-22 1999-05-17 Sieving device for solid material and a method for sieving solid material

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KR20010034887A (en) 2001-04-25
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PT1348492E (en) 2004-12-31
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CZ20004228A3 (en) 2001-08-15
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WO1999061172A2 (en) 1999-12-02
CN1268447C (en) 2006-08-09
ATE260715T1 (en) 2004-03-15
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EP1144137A2 (en) 2001-10-17
EP1348492B1 (en) 2004-07-28
EP1144137A3 (en) 2002-11-20
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WO1999061172A3 (en) 2002-10-03
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US6786335B1 (en) 2004-09-07
CN1530182A (en) 2004-09-22
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CA2333051A1 (en) 1999-12-02
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DK1348492T3 (en) 2004-12-06
PT1144137E (en) 2004-07-30
DE59910086D1 (en) 2004-09-02

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