WO2012171597A1 - Vorrichtung zum mechanischen aufschliessen von konglomeraten aus materialien unterschiedlicher dichte und/oder konsistenz - Google Patents
Vorrichtung zum mechanischen aufschliessen von konglomeraten aus materialien unterschiedlicher dichte und/oder konsistenz Download PDFInfo
- Publication number
- WO2012171597A1 WO2012171597A1 PCT/EP2012/001603 EP2012001603W WO2012171597A1 WO 2012171597 A1 WO2012171597 A1 WO 2012171597A1 EP 2012001603 W EP2012001603 W EP 2012001603W WO 2012171597 A1 WO2012171597 A1 WO 2012171597A1
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- Prior art keywords
- rotor
- digestion chamber
- sections
- chamber
- impact
- Prior art date
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Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B02—CRUSHING, PULVERISING, OR DISINTEGRATING; PREPARATORY TREATMENT OF GRAIN FOR MILLING
- B02C—CRUSHING, PULVERISING, OR DISINTEGRATING IN GENERAL; MILLING GRAIN
- B02C13/00—Disintegrating by mills having rotary beater elements ; Hammer mills
- B02C13/14—Disintegrating by mills having rotary beater elements ; Hammer mills with vertical rotor shaft, e.g. combined with sifting devices
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B02—CRUSHING, PULVERISING, OR DISINTEGRATING; PREPARATORY TREATMENT OF GRAIN FOR MILLING
- B02C—CRUSHING, PULVERISING, OR DISINTEGRATING IN GENERAL; MILLING GRAIN
- B02C13/00—Disintegrating by mills having rotary beater elements ; Hammer mills
- B02C13/20—Disintegrating by mills having rotary beater elements ; Hammer mills with two or more co-operating rotors
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B02—CRUSHING, PULVERISING, OR DISINTEGRATING; PREPARATORY TREATMENT OF GRAIN FOR MILLING
- B02C—CRUSHING, PULVERISING, OR DISINTEGRATING IN GENERAL; MILLING GRAIN
- B02C13/00—Disintegrating by mills having rotary beater elements ; Hammer mills
- B02C13/26—Details
- B02C13/282—Shape or inner surface of mill-housings
Definitions
- the invention relates to a device for the mechanical breaking up of conglomerates of materials with different density and / or consistency.
- Such a device may, for. B. be used in waste recycling.
- slags that are produced during metal production, and in other slags and ashes, which can be fed to a thermal waste, are regularly iron and other metals. These can be heavily scaled or embedded in dainty form in mineral slags.
- the metals from the composites or scalings must be digested so that they can subsequently be separated from magnets by means of magnets or separators for non-ferrous metals or other sorting systems. From the prior art, it is known to crush such slags with hammer mills or impact mills and then supply for actual separation magnets or separators for non-ferrous metals.
- the invention is therefore based on the object of proposing a device for the mechanical disintegration of conglomerates of materials with different density and / or consistency, which allows a mechanical disruption or separation of small and smallest bound in slag solid metal particles.
- the proposed device should also be suitable for breaking up other conglomerates of materials of different density and / or consistency. This object is achieved by a device with the
- the device according to the invention has a digestion chamber with a
- Feed opening at a first end and with an outlet opening at a second end is surrounded by a cylindrical or truncated cone-shaped digestion chamber wall, which is typically oriented vertically, with the feed side at the top and the outlet side at the bottom. In such a vertical arrangement, a
- the disruption chamber has at least two, preferably three successive sections. In each of these sections, in each case at least one rotor with a rotor shell and, at least in an operating state, striking tools extending radially from the rotor shell into the disruption chamber are arranged. If z. B. chains are used as impact tools, these of course only extend radially into the digestion chamber, when the corresponding rotor rotates sufficiently fast. Such impact tools are also referred to as impact tools extending radially from the rotor shell into the disruption chamber. With the striking tools conglomerates can be broken in the manner described below, possibly in conjunction with baffles described below at the digestion chamber wall.
- the rotors in the successive sections each have a rotor shell having a radius increasing toward the second end of the disruption chamber, wherein a difference between the radius of the respective rotor shell and a radius of the disruption chamber wall decreases from the first end to the second end.
- the rotor shells of the rotors thus have more or less the shape of a cone in the successive sections, which has an increasing radius from the first end to the second end.
- Said cone can have a continuously increasing diameter in the manner of a cone towards the second end or else a stepwise, for example cascading, increasing diameter.
- the digestion chamber wall can either have a constant or a radius increasing from the feed opening to the outlet opening. The latter also causes velocities of particles that travel through the digestion chamber to increase with increasing distance traveled. It is not excluded that the radius of the digestion chamber wall from the first End decreases to the second end. In the event that the radius of the digestion chamber wall increases towards the typically lower second end, this radius can change either continuously or stepwise. In any case, the radius of the respective rotor shell and the radius of the disruption chamber wall are chosen so that a difference between these two radii decreases in the axial direction from the first end to the second end.
- the material which is supplied at the first end and flows through the digestion chamber wall becomes less and less volume as it progresses axially through the digestion chamber, as a result of which a particle density and hence a frequency of mutual impacts and impacts of the particles against the impact tools or Baffles is increased.
- the rotors in each adjacent sections preferably have an opposite direction of rotation. This allows the particles, which are accelerated by the impact tools in one of the sections, to impact the counter-rotating impact tools head-on in the next section. This leads to impact velocities, which result in each case as the sum of particle velocity and velocity of impact tools.
- the conglomerates can be broken if they contain materials of different density and / or different consistency, for example, different elasticity.
- rotational speeds of the rotors preferably increase in the various portions from the first end to the second end of the digestion chamber. This can also have the consequence that the impact velocities in the region of increasing particle density increase towards the second end of the disruption chamber, because there are also increasing speeds of the impact tools with the increasing rotational speeds of the rotors.
- the speed of the conglomerates brought into the digestion chamber through the feed opening increases greatly, as does the particle density, towards the outlet opening. This can lead to conglomerates with velocity in the last section of the digestion chamber in front of the outlet opening. of z. B. bounce over 200 m / s against baffles or impact tools. In this way, the conglomerates can be broken up without being ground as in conventional hammer mills or impact mills. Thus, metal particles contained in particular in the conglomerates can be dissolved out without these being undesirably comminuted in their turn.
- the proposed device thus allows a digestion of metals, such as iron or non-ferrous metals, from slags or scaling in a way that is not possible with the conventional hammer mills or impact mills.
- the proposed device is based on a construction by which an impact energy réellestalden conglomerates is maximized in their impact on the striking tools and / or baffles, but at the same time a crushing of the metal parts itself is prevented. This means that even very small metal parts in slag can still be economically opened up and separated. With the invention, therefore, extremely high impact velocities of conglomerates to be grown are achieved, wherein the conglomerates are broken up with a very low grinding action.
- the rotor in each of the sections has its own drive which is operable or controllable independently of the drive or drives of the at least one other section. This allows an individual adjustment of rotational speeds of the rotors to different réelleumblede conglomerates.
- the rotor shell is preferably frusto-conical.
- the rotor shells of the rotors in the successive sections of the digestion chamber form a truncated cone, wherein the diameter of the immediately successive truncated cones at their ends facing each other preferably equal, so that the rotor shells of the different rotors together in turn a conical or frusto-conical shape form.
- the metal particles from the supplied material conglomerates in the entire digestion chamber in each case be transferred into radially outer regions, without thereby a material throughput in the axial direction of the digestion chamber would be significantly reduced.
- the diameters of the rotor sheath or the rotor shells may also increase gradually, then preferably in each of the sections one or more axially successive areas are provided in which there is a constant diameter of the rotor shell, wherein the rotor shell in subsequent areas has gradually larger diameters , In this case, however, a material throughput through the digestion chamber in the axial direction is more severely impaired.
- the striking tools are kept interchangeable in receptacles provided on the rotor, so that they are easily replaceable.
- the rotor shells are preferably also formed in the same way from a plurality of rotor sheath elements which are held interchangeably on the respective rotor. Namely, wear of the rotor shells is to be expected because they are exposed to many shocks when the particles are transported out of the conglomerate through the respective rotor shell to the outside. An exchange of individual possibly damaged rotor sheath elements is associated with significantly lower costs than a replacement of the entire rotor.
- the proposed device will be explained with reference to a digestion chamber with three sections. However, the device could also be realized with only two sections or four or even a larger number of sections and work in a similar manner.
- a first section of the digestion chamber viewed from the first end or from the feed opening, is called here a pretreatment chamber.
- This pretreatment chamber is followed in the direction of the second end by a second section, which may be referred to as an acceleration chamber.
- a remaining third section, which is closest to the second end or to the outlet opening, is referred to as a high-speed impact chamber.
- first section and / or in the second section and / or in the third section of the digestion chamber in each case two or more staggered in the axial direction receptacles are provided for the striking tools.
- a number of striking tools in each of the sections can be set within wide limits. This brings in the first two sections a better acceleration of the particles and conglomerates and in the third section a greater likelihood of a controlled impact of the conglomerate or the particles on a percussion tool with it.
- the rotor casing can have entrainment bars that extend axially and radially into the digestion chamber.
- the number of collisions of the particles or conglomerates in the digestion chamber may be increased by baffles disposed axially and radially inwardly of the digestion chamber wall. As a result, accelerated by the impact tools particles can bounce against these baffles and break it up.
- the number of impact tools in the pre-treatment chamber may be even lower because the pretreatment chamber has the task of conveying the particles of the conglomerate outwardly in the radial direction to reach an area where the impact tools of the subsequent acceleration chamber are effective. Therefore, more impact tools should be placed in the acceleration chamber.
- carrier strips can be provided on the rotor shell in the pretreatment chamber, which serve for effective transport of the particles into the region lying radially further outward.
- Impact tools accelerate the particles, which are present in increasing density toward the second end, toward the outside and toward the second end, ie typically downwards, in the direction of the high-speed impact chamber.
- Mitauerraun can also be provided on the rotor shell of the rotor in the acceleration chamber, which can also serve to transfer the particles in more remote areas. There they can be greatly accelerated by the more numerous percussion tools in the accelerator chamber while simultaneously moving toward the high velocity impact chamber.
- Most striking tools are preferably provided in the third section, that is in the high-speed impact chamber. These impact tools have the purpose of breaking up the particles which are present there in an increased particle density due to the increasing diameter of the rotor shell with the highest possible probability in this section of the disruption chamber.
- the rotational speed of the striking tools and the corresponding rotor is preferably highest in the high speed impaction chamber. It can be chosen so that the speed of the striking tools there in outer areas is above 200 m / s, but preferably below 300 m / s, ie in particular below the speed of sound.
- the rotational speed of the rotor in one of the sections for rotational speed of the rotor in the section arranged in the direction towards the first end is a ratio of between 1: 1 and 5: 1, preferably a ratio of between 2: 1 and 4: 1 has. It turns out that so both the
- Impact velocity and the probability of impact of a metal particle or a metal-containing particle can be maximized on a percussion tool.
- the rotational speed of the rotor in the last section facing the second end is selected such that an absolute velocity of outer edges of the striking tools is between 100 m / s and 300 m / s, preferably between 130 m / s and 200 m / s or between 200 m / s and 300 m / s.
- the radius of the rotor shell to the radius of the digestion chamber wall in the first section has a ratio of between 0.15 and 0.5.
- the radius of the rotor shell preferably has a ratio of between 0.34 and 0.65 to the radius of the digestion chamber wall.
- the corresponding ratio is preferably between 0.55 and 0.85.
- a speed of the striking tools is greater than in areas further in the interior.
- the diameter of the rotor shells in the digestion chamber may increase from top to bottom, for example from 500 mm or 600 mm to 1400 mm or 1500 mm. It may be provided that the diameter of the digestion chamber wall at the same time increases from about 1200 mm or 1300 mm above to an amount of about 1900 mm below or remains constant in a range of between 1700 mm and 1900 mm. In any case, a distance between the respective rotor shell and the digestion chamber wall decreases from the first end to the second end. Under certain circumstances, it may be sufficient if such a decrease exists at least on average over a certain distance in the axial direction of the dissolution chamber.
- Rotors can in the example described with three sections z. B. 500 revolutions per minute or 600 revolutions per minute for the rotor in the first section, 900 revolutions per minute or 600 revolutions per minute for the rotor in the second section and 1400 revolutions per minute or 1500 revolutions per minute for the rotor in the third
- the rotor rotates in the third section in opposite directions to the rotors in the first and second sections, while the rotors in the first and in the second section have the same direction of rotation.
- speeds of impact tools in outer areas of the third section ie in the high-speed impact chamber, can be achieved above 140 m / s.
- impact speeds of over 200 m / s can be achieved.
- the impact velocity, and hence the impact energy, of the metal particles or metal-containing particles of the conglomerate may be controlled and maximized upon impact with the impact tools and / or baffles within reasonable physical limits.
- the striking tools can z. B. be formed by chains and / or blow bars or chains and / or blow bars. Such impact tools are z. B. from the document DE 10 2005 046 207 AI known per se.
- the device preferably has a feed hopper at the first end of the digestion chamber and / or an output hopper at the second end of the digestion chamber.
- the mechanically schllos sene material z. B. directed onto a conveyor belt or fed to a Abscheidungsvor- direction.
- the device described can not be used exclusively for digesting metal particles in slags. Rather, it can also be used to unlock all other types of material conglomerates consisting of materials of different density and / or elasticity.
- the disruption chamber wall and / or impact tools and / or the rotor shells are formed of hard (,) impact resistant materials such as metal or ceramic-metal composites.
- one or more or all sections of the disruption chamber not only one rotor, but two or more rotors are provided, which follow one another in the axial direction.
- the number of sections may vary and in particular be two, three, four or five, or even greater.
- the digestion chamber wall has a plurality of annularly extending inwardly pointing projections in order to divert material falling downwards along the digestion chamber wall in the direction of the interior of the digestion chamber, so that this
- Material can be reached again by the striking tools.
- the falling material can be brought back into an area of impact of the impact tools to be unlocked effectively.
- Fig. 1 shows a partially sectioned longitudinal section through a device for
- FIG. 2 shows a longitudinal section of a detail of the device from FIG. 1, FIG.
- FIG. 3 shows a cross section of another detail of this device with a suspension of a striking tool
- Fig. 5 is a sectional view of another detail of the apparatus of Fig. 1 and
- Fig. 6 shows a schematic representation of a feasible by this device digestion of a conglomerate.
- a device 1 for the mechanical digestion of conglomerates of materials of different density and / or consistency is shown as a partially sectioned longitudinal section.
- the device 1 has a digestion chamber with a cylindrical digestion chamber wall 2, which is arranged vertically and has a constant diameter. However, it would also be possible that this diameter z. B. increases from top to bottom.
- a rotor assembly 3 is centered arranged. This has three superposed rotors 4, 5, 6, which can be driven separately.
- Portions of the cylindrical digestion chamber wall 2 are a first section 7, a second section 8 and a third section 9 of the digestion chamber.
- the upper first section 7 of the digestion chamber is a pretreatment chamber, the central second section 8 an acceleration chamber and the lower third section 9 in front of an outlet opening 10 a high-speed impact chamber.
- the digestion chamber has a feed opening 14, there being provided a feed hopper 15 for the conglomerate to be supplied as bulk material to be separated.
- an output funnel 16 At the lower end of the digestion chamber with the sections 7, 8, 9 is an output funnel 16, with which the comminuted and mechanically digested bulk material z.
- a belt conveyor can be supplied.
- the rotors 4, 5, 6 each have a frustoconical rotor shell 17, 18, 19.
- the rotor shells 17, 18, 19 are arranged concentrically to the respective rotor 4, 5, 6 and have an increasing from top to bottom
- Diameter so that the rotor assembly 3 or more precisely the shape formed by the three rotor shells 17, 18, 19 is a total of frustoconical.
- the individual rotors and sections are subsequently numbered from top to bottom in the direction of the flow of material.
- the first rotor 4 has in the axial direction offset relative to each other two circumferentially distributed rows of striking tools 20, 21. These are connected to the first rotor 4 in a manner described in more detail below.
- the second rotor 5 has a third and fourth row of impact tools 22, 23, which are also arranged offset in the axial direction relative to each other.
- the third rotor 6 also has two rows of impact tools 24, 25 displaced relative to one another in the axial direction on.
- These impact tools 20, 21, 22, 23, 24, 25 are chains and / or metal rods, which have a hard metal edge at their outer end and on their front side in the direction of rotation.
- the diameter of the rotor shells 17, 18, 19 of the rotor assembly 3 decreases from top to bottom continuously in the manner of a truncated cone.
- the diameter of the digestion chamber wall 2 is constant in the present embodiment.
- the digestion chamber wall 2 has a plurality of annular circumferential projections 26, which are arranged offset relative to one another in the axial direction. These projections 26 serve the purpose of diverting particles that fall down on the digestion chamber wall 2 inwardly, ie on the rotor 4, 5, or 6, so that they can effectively be comminuted by mechanical disruption. Unlike shown here, the
- Projections 26 also be chamfered from the top to the bottom inside. Thus, the described conductive effect can be achieved even better.
- the digestion chamber wall 2 unlike in the case shown here, has a radius increasing from top to bottom, the annular projections 26 are not necessary.
- the inner diameter of the disruption chamber wall 2 can be, for example, 1800 mm, while the inner diameter of the annular peripheral projections 26 is smaller and, for example, 1700 mm.
- the first Rotormantesl 17 whose diameter z. B. 700 mm
- the lower third rotor shell 19 at its lower end has a diameter of, for example, 1300 mm.
- the gap between digestion chamber wall 2 and rotor shell 17, 18, 19 thus decreases from the upper end to the lower end from 550 mm to 250 mm.
- the distance between the rotor shells 17, 18, 19 and the corresponding portion of the digestion chamber wall 2 decreases from top to bottom and displaces radially outwards.
- an effective digestion of the supplied conglomerates is supported.
- this reduces the volume of the digestion chamber 2 per Wgumble downwards, resulting in a downwardly increasing density of the material in the digestion chamber results.
- the supplied material is thereby transferred into a further outward radial region of the disruption chamber of the device 1, where the speed of the striking tools 20, 21, 22, 23, 24, 25 is greater.
- the first two rotors 4, and 5 are driven so that they rotate in the same direction, while a direction of rotation of the third rotor 6 is in opposite directions.
- the accelerated by the striking tools 22, 23 of the second rotor 5 material therefore meets the rotating in the opposite direction striking tools 24, 25 of the third rotor 6.
- the three rotors 4, 5 ( 6 are driven by drives from above via concentrically supported shafts 11, 12, 13.
- the shafts 11, 12, 13 can also extend downwards and be driven from below the drives themselves can be arranged within the rotor shells 17, 18, 19 of the corresponding rotors 4, 5, 6. In that case, it is unnecessary to lead out drive shafts from the disruption chamber.
- FIG. 2 a detail of the upper first rotor 4 of the device 1 from FIG. 1 is shown by way of example.
- the first rotor has three plate receptacles 27, 28, 29, the rotatably connected to the associated shaft 11 are not shown here and rotate with it.
- the outer plate receptacle 27 has a smaller outer diameter than the underlying plate receptacles 28 and 29.
- An outer periphery of the upper two plate receptacles 27, 28 has recesses 30, are inserted into the first members 31 of percussion chains, which are each held by a bolt 32 ,
- pockets 33 are provided in the plate receptacles 27, 28. This is shown in Fig. 4 using the example of the plate holder 28 and one of the striking tools 21.
- the aforementioned impact chains form part of the corresponding striking tool 20 or 21.
- All plate receptacles 27, 28, 29 of the rotor 4 have vertical holes through which bolts 34,35 can be pushed. Between each two of the plate receptacles 27, 28 and 28, 29 rotor shell elements 36, 37 are arranged. These also have vertical holes 38 which are aligned with the holes of the plate seats 27, 28, 29.
- the rotor shell elements 36, 37 facing 28 stops 39, 40, 41 are formed on an underside of the upper Tell matter 27 and on an upper side of the underlying plate receptacle 28 and on the underside of this plate receptacle. At these comes the shaft 11 facing side of horizontal support walls of the rotor shell elements 36, 37 to lie.
- the rotor sheath elements 36, 37 are centered and held in the correct position relative to the rotor 4 and supported.
- the rotor shell elements 36, 37 are then fixed to the rotor 4 in the position thus determined. If the rotor sheath elements 36, 37 are to be replaced, this can be done in a simple manner by removing the bolts 34, 35 and exchanging the corresponding rotor sheath elements 36, 37.
- the downstream rotor shell element 37 has a
- Carrier strip 42 which extends radially and axially from a frustoconical outer surface of the rotor shell member 37 to the outside. With the Mitauer 42, the reaching into the region of the rotor shell 17 particles can be accelerated radially outward, so that they get into the area, so the impact tools 20, 21, 22, 23, 24, 25 have higher speeds.
- the driver strips 42 are also provided in particular on corresponding rotor shell elements of the second rotor 5.
- the lower rotor shell element 37 on an outer edge 43 which engages over the bottom plate receptacle 29 of the rotor 4 and which is supported against the plate receptacle 29 and thus in a similar manner as the stops 39, 40, 41, the respective rotor shell element 37 on the rotor 4 in her Position helps where it is then fixed by the bolts 35.
- the receptacle 45 for the respective percussion tools 22 and the bore for the corresponding pin 46 are here radially further out.
- Figures 3 and 4 show the example of the plate holder 28, as the
- Plate receptacles 27, 28, 44 are connected to the striking tools designed as impact chains 20, 21, 22, 23, 24, 25.
- the striking tools 20, 21, 22, 23, 24, 25 each have a first chain link 31, facing the respective rotor 4, 5 or 6, in which the vertical bolt 32 is welded.
- first chain link 31 engages a second semi-open chain link 47, in which a further part of the striking tool 20, 21, 22, 23, 24, 25 is welded from a very wear-resistant steel.
- Tellernessn 27, 28, 29 are distributed over the circumference several -. B. up to eight - milled pockets 33, in which the striking tools are hung with the bolt 32.
- Fig. 3 one of the annular circumferential projections 26 of the digestion chamber wall 2 can be seen, which is opposite to the impact tool 21. These projections 26 can also be beveled on an upper side in order to better guide particles falling there into the region of the striking tools 21, 22, 23, 24, 25.
- FIG. 5 shows a detail of the device 1 from FIG. 1, which shows how a baffle element 49 is fastened in the digestion chamber wall 2.
- the impact element 49 has a baffle surface 50 which serves as an impact surface for the material accelerated by the impact tools 20, so that metal conglomerates can be broken there.
- the conglomerates are of course also on the striking tools 20 and the other striking tools 21, 22, 23, 24, 25 self-digested.
- the direction of rotation of the rotor 4 with the impact tool 20 is shown in Fig. 5 by an arrow.
- the impact elements 49 form a toothing projecting on the digestion chamber wall 2 into the digestion chamber with the rotors 4, 5, 6 by extending axially and radially inwards into the digestion chamber.
- the baffles 49 are inserted into pockets 51 provided for this purpose. These are distributed over a circumference of the digestion chamber wall 2. So z. B. four or eight or much more pockets 51 may be distributed with impact elements 49 around the circumference.
- the baffles 49 can be inserted from the outside into the pockets 51 and then screwed to an outer side of the digestion chamber wall 2. The direction of rotation facing in the disruption chamber 2 protruding side of the impact member 49 forms the aforementioned baffle 50.
- a smooth cylindrical digestion chamber wall 2 without such baffles 50 is desired, instead placeholder 52 can be inserted into these pockets 51.
- the placeholder 52 have the same thickness as the digestion chamber wall 2 including a Schl adoptedausposed 53 of the digestion chamber wall 2. Therefore, the placeholder 52 are aligned with the inner digestion chamber chamber wall aligned, resulting in a consistently smooth cylindrical inner surface 54 of the digestion chamber wall 2.
- the baffles 49 protrude into the Digestion chamber into it.
- Fig. 6 illustrates schematically the operation of the device 1 with the digestion device according to the present invention. Conglomerates 55, which consist of metal particles 56 and Schlackeresten 57 are accelerated by the impact tools 20, 21, 22, 23 of the device 1. This gives you a speed v 2 .
- the number and the distribution of the impact tools 20, 21, 22, 23, 24, 25 may differ from the illustrated embodiment.
- other impact tools in particular chains and impact strips, can also be used.
- many more impact tools can be distributed over the circumference than in the first section 7.
- this leads to an increased Probability of collisions. It can be provided that a sector of the digestion chamber wall 2 is to be opened in order, for. B. to allow access to the digestion chamber 2 for maintenance.
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Abstract
Description
Claims
Priority Applications (4)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2014513062A JP6159718B2 (ja) | 2011-06-01 | 2012-04-04 | 密度および/またはコンシステンシーの異なる物質を含む集合体の機械的分離装置 |
| CN201280029359.0A CN103648652B (zh) | 2011-06-01 | 2012-04-04 | 用于从不同密度和/或坚度的材料机械地分离聚块的设备 |
| RU2013157304/13A RU2596758C2 (ru) | 2011-06-01 | 2012-04-04 | Устройство для механического разделения конгломератов, состоящих из материалов с разными плотностями и/или консистенциями |
| CA2837763A CA2837763C (en) | 2011-06-01 | 2012-04-04 | Device for mechanical separation of conglomerates from materials of different densities and/or consistencies |
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| DE102011050789A DE102011050789A1 (de) | 2011-06-01 | 2011-06-01 | Vorrichtung zum mechanischen Trennen von Materialkonglomeraten aus Materialen unterschiedlicher Dichte und/oder Konsistenz |
| DE102011050789.2 | 2011-06-01 |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| WO2012171597A1 true WO2012171597A1 (de) | 2012-12-20 |
Family
ID=46318869
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| PCT/EP2012/001603 Ceased WO2012171597A1 (de) | 2011-06-01 | 2012-04-04 | Vorrichtung zum mechanischen aufschliessen von konglomeraten aus materialien unterschiedlicher dichte und/oder konsistenz |
Country Status (10)
| Country | Link |
|---|---|
| US (1) | US8777142B2 (de) |
| EP (1) | EP2529835B1 (de) |
| JP (1) | JP6159718B2 (de) |
| CN (1) | CN103648652B (de) |
| CA (1) | CA2837763C (de) |
| DE (1) | DE102011050789A1 (de) |
| DK (1) | DK2529835T3 (de) |
| HU (1) | HUE045830T2 (de) |
| RU (1) | RU2596758C2 (de) |
| WO (1) | WO2012171597A1 (de) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| EP2837424A1 (de) * | 2013-08-13 | 2015-02-18 | TARTECH eco industries AG | Schlackenbrecher |
| DE102016110086A1 (de) | 2016-06-01 | 2017-12-07 | TARTECH eco industries AG | Vorrichtung zum Auftrennen von Konglomeraten, die aus Materialien unterschiedlicher Dichte bestehen |
| WO2018224118A1 (de) | 2017-06-04 | 2018-12-13 | TARTECH eco industries AG | Vorrichtung zum auftrennen von konglomeraten, die aus materialien unterschiedlicher dichte bestehen |
Families Citing this family (17)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE102012104031B4 (de) * | 2012-05-08 | 2017-05-04 | Pms Handelskontor Gmbh | Trennvorrichtung für Materialkonglomerate |
| SK288377B6 (sk) * | 2012-12-14 | 2016-07-01 | Plesnăťk Juraj | Chumáčovina ako konštrukčný materiál, najmä pre stavebníctvo, spôsob jej výroby a zariadenie na jej výrobu |
| DE102013110352A1 (de) * | 2013-09-19 | 2015-03-19 | Pms Handelskontor Gmbh | Zerkleinerungsvorrichtung |
| JP6059651B2 (ja) * | 2013-12-17 | 2017-01-11 | ヨシワ工業株式会社 | 破砕分離装置 |
| US10376894B2 (en) | 2014-02-14 | 2019-08-13 | Glennon C. Sontag | Grinder |
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Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| EP2837424A1 (de) * | 2013-08-13 | 2015-02-18 | TARTECH eco industries AG | Schlackenbrecher |
| DE102016110086A1 (de) | 2016-06-01 | 2017-12-07 | TARTECH eco industries AG | Vorrichtung zum Auftrennen von Konglomeraten, die aus Materialien unterschiedlicher Dichte bestehen |
| DE102016110086B4 (de) | 2016-06-01 | 2019-09-26 | TARTECH eco industries AG | Vorrichtung zum Auftrennen von Konglomeraten, die aus Materialien unterschiedlicher Dichte bestehen |
| WO2018224118A1 (de) | 2017-06-04 | 2018-12-13 | TARTECH eco industries AG | Vorrichtung zum auftrennen von konglomeraten, die aus materialien unterschiedlicher dichte bestehen |
Also Published As
| Publication number | Publication date |
|---|---|
| JP2014527457A (ja) | 2014-10-16 |
| RU2596758C2 (ru) | 2016-09-10 |
| US8777142B2 (en) | 2014-07-15 |
| HUE045830T2 (hu) | 2020-01-28 |
| RU2013157304A (ru) | 2015-07-20 |
| US20120325949A1 (en) | 2012-12-27 |
| JP6159718B2 (ja) | 2017-07-05 |
| CA2837763C (en) | 2016-12-13 |
| EP2529835B1 (de) | 2019-05-01 |
| DK2529835T3 (da) | 2019-08-05 |
| CN103648652A (zh) | 2014-03-19 |
| CA2837763A1 (en) | 2012-12-20 |
| EP2529835A3 (de) | 2017-11-22 |
| CN103648652B (zh) | 2016-02-17 |
| EP2529835A2 (de) | 2012-12-05 |
| DE102011050789A1 (de) | 2012-12-06 |
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