EP1448303B1 - Tube grinder and method for comminuting lumpy grinding stock - Google Patents
Tube grinder and method for comminuting lumpy grinding stock Download PDFInfo
- Publication number
- EP1448303B1 EP1448303B1 EP02787865A EP02787865A EP1448303B1 EP 1448303 B1 EP1448303 B1 EP 1448303B1 EP 02787865 A EP02787865 A EP 02787865A EP 02787865 A EP02787865 A EP 02787865A EP 1448303 B1 EP1448303 B1 EP 1448303B1
- Authority
- EP
- European Patent Office
- Prior art keywords
- grinding
- tube mill
- grinding chamber
- chamber
- material quantity
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Lifetime
Links
- 238000000227 grinding Methods 0.000 title claims description 150
- 238000000034 method Methods 0.000 title claims description 16
- 238000005192 partition Methods 0.000 claims description 22
- 238000007599 discharging Methods 0.000 claims 4
- 238000012216 screening Methods 0.000 claims 3
- 238000003801 milling Methods 0.000 description 2
- 230000003068 static effect Effects 0.000 description 2
- 230000001419 dependent effect Effects 0.000 description 1
- 238000010422 painting Methods 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 238000011144 upstream manufacturing Methods 0.000 description 1
Images
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
- B02C21/00—Disintegrating plant with or without drying of the material
- B02C21/002—Disintegrating plant with or without drying of the material using a combination of a roller mill and a drum mill
- B02C21/005—Disintegrating plant with or without drying of the material using a combination of a roller mill and a drum mill the roller mill having cooperating rollers
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B02—CRUSHING, PULVERISING, OR DISINTEGRATING; PREPARATORY TREATMENT OF GRAIN FOR MILLING
- B02C—CRUSHING, PULVERISING, OR DISINTEGRATING IN GENERAL; MILLING GRAIN
- B02C17/00—Disintegrating by tumbling mills, i.e. mills having a container charged with the material to be disintegrated with or without special disintegrating members such as pebbles or balls
- B02C17/04—Disintegrating by tumbling mills, i.e. mills having a container charged with the material to be disintegrated with or without special disintegrating members such as pebbles or balls with unperforated container
- B02C17/06—Disintegrating by tumbling mills, i.e. mills having a container charged with the material to be disintegrated with or without special disintegrating members such as pebbles or balls with unperforated container with several compartments
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B02—CRUSHING, PULVERISING, OR DISINTEGRATING; PREPARATORY TREATMENT OF GRAIN FOR MILLING
- B02C—CRUSHING, PULVERISING, OR DISINTEGRATING IN GENERAL; MILLING GRAIN
- B02C17/00—Disintegrating by tumbling mills, i.e. mills having a container charged with the material to be disintegrated with or without special disintegrating members such as pebbles or balls
- B02C17/18—Details
- B02C17/183—Feeding or discharging devices
- B02C17/1835—Discharging devices combined with sorting or separating of material
- B02C17/184—Discharging devices combined with sorting or separating of material with separator arranged in discharge path of crushing zone
- B02C17/1845—Discharging devices combined with sorting or separating of material with separator arranged in discharge path of crushing zone with return of oversize material to crushing zone
Definitions
- the invention relates to a tube mill and a method for crushing lumpy material.
- Tube mills in particular ball mills, are well known. They essentially consist of a first grinding chamber, at least one second grinding chamber and a co-rotating intermediate wall arranged between the grinding chambers. They are used for shredding different materials in various industrial sectors.
- the material to be crushed is comminuted during the grinding process of the freely movable MahlSystem sectionung inside the grinding chamber, being used as a grinding body both spherical and rod or rod-like body.
- the intermediate walls in the tube mills serve the purpose of separating the grinding media filling of adjacent grinding chambers from one another and to transport the material being ground in a controlled manner from one to the other grinding chamber.
- a discharge device is usually arranged in the intermediate wall, through which the grist received via entry openings into the intermediate chamber is discharged via a discharge opening into the second grinding chamber.
- the invention is based on the object to improve the efficiency of a tube mill and a method for crushing lumpy material to be ground.
- the inventive method for crushing lumpy material to be ground with a tube mill containing at least a first and a second grinding chamber and a co-rotating between the grinding chambers mitrotierende intermediate wall, the comminuted in the first grinding chamber millbase is divided in an intermediate wall in a first and a second Mahlgutteilmenge, wherein at least a portion of the second Mahlgutteilmenge passes directly or indirectly into the second grinding chamber and at least the first Mahlgutteilmenge is discharged separately from the tube mill.
- the separating device is formed by a classifying device, so that the first Mahlgutteilmenge consists of coarse material and the second Mahlgutteilmenge consists of fine material.
- the classifier can be formed, for example, by a sieve or trench wall, a drum screen or Siebhubschaufeln.
- the discharged first Mahlgutteilmenge can be wholly or partially fed to the Mahlgutiergabe the first grinding chamber or a Vormahlaggregat.
- the tube mill shown essentially consists of a first grinding chamber 1, a second grinding chamber 2 and a co-rotating intermediate wall 3 arranged between the grinding chambers.
- the material to be ground 4 passes through a material feed 5 into the first grinding chamber 1, in which it is rotated about a longitudinal center axis by rotation of the tube mill 6 comes to shredding.
- both grinding chambers contain so-called grinding media, which are adapted in shape, size, quantity and material to the respective needs.
- the first grinding chamber is usually separated from the intermediate wall 3 by a slot wall 3.4, which has openings 3.5, through which the ground material sufficiently comminuted in the first grinding chamber reaches a first intermediate wall region 3.1.
- the intermediate wall 3 has, in addition to the first intermediate wall region 3.1, a second intermediate wall 3.3, wherein the two intermediate wall regions are separated from one another by a classifying device 3.2.
- the integrated classifying device 3.2 divides the material to be ground from the first grinding chamber into a coarse material 8 consisting of first Mahlgutteilmenge and a fine material consisting of 9 second Mahlgutteilmenge.
- the fine material 9 passes into the second intermediate wall region 3.3 and is there via suitable means, such as lifting elements, the second grinding chamber 2 fed.
- the coarse material 8 obtained within the classifying device 3.2 is discharged from the tube mill and can be returned to the grinding process at a suitable point (preferably at the grinding stock inlet 4).
- the classifying device 3.2 is designed as a screen or diaphragm wall.
- the first partition wall area 3.1 is thereby bounded by the slot wall 3.4 and the classifying device 3.2 and the second partition wall area 3.3 by the classifying device 3.2 and the partition wall 3 separating from the second grinding chamber 2 end wall 3.6.
- the fine material 9 coming from the first grinding chamber 1 via the opening 3.5 into the first intermediate wall region 3.1 passes unhindered via the classifying device 3.2 into the second intermediate wall region 3.3 and is discharged there via a discharge device (not illustrated in particular lifting blades) into the second grinding chamber 2.
- the coarse material 8 introduced from the first grinding chamber 1 into the first intermediate wall area 3.1 remains in front of the classifying device 3.2, wherein the coarse material level gradually rises in the first intermediate wall area until it has reached a certain height, at which the coarse material 8 enters a discharge opening 3 within the classifying device 3.2 arranged discharge 3.8 arrived.
- About an outlet channel 3.9 the coarse material 8 is discharged through a discharge 3.11 from the tube mill.
- the height of the level of the coarse material 8 can be adjusted in front of the classifying device 3.2 by varying the radial distance of the discharge opening 3.10 from the longitudinal central axis 6.
- the amount of coarse material 8 discharged can be adjusted by varying the size of the discharge opening 3.10.
- Fig. 2a-2e is a tube mill with an intermediate wall 10 according to a second embodiment.
- the intermediate wall 10 is divided into at least one, preferably, but several Siebkammem, which are arranged like a segment around the longitudinal central axis 6.
- Each screen chamber is bounded by radial side walls 10.9, 10.10 and a part of the first grinding chamber 1 facing slot wall 10.4 and a part of the second grinding chamber 2 facing end wall 10.6.
- Fig. 2b shows a view of belonging to an intermediate wall chamber portion of the slot wall 10.4.
- Each intermediate wall chamber is subdivided into a first intermediate wall chamber 10. 1 and a second intermediate wall chamber 10. 3 by a sieve lifting vane 10. 2 designed as a sieve.
- the inlet openings 10.5 of the slot wall 10.4 are provided only in the region of the first partition wall chamber 10.1, so that the ground in the grinding chamber 1 regrind enters through the inlet openings 10.5 in the first partition chamber 10.1.
- the material to be ground in the first intermediate wall chamber 10.1 is raised above the sieve lifting blades 10.2.
- the fine material 9 contained in the material to be ground passes through the sieve openings of Siebhubschaufeln 10.2 in the second partition wall portion 10.3 and is passed there via a Feingutabweisblech 10.11 in the second grinding chamber.
- the coarse material 8 runs over the Siebhubschaufeln 10.2 and is then promoted via a Grobgutabweisblech 10.12 in a shaft 10.7.
- About the mill rotation located in the shaft 10.7 Grobgut 8 is discharged from the tube mill.
- FIG. 3a and 3b variant shown shows an intermediate wall 11, in which the separating or classifying device is formed by a sieve drum 11.2, which divides the intermediate wall into an inner first intermediate wall region 11.1 and an outer second intermediate wall region 11.3.
- the ground material passes through inlet openings in the slot wall 11.4 in the first intermediate wall region of the screen drum 11.2.
- the fine material 9 falls through the sieve drum in the second partition wall area 11.3.
- the coarse material 8 is collected in Grobgutaustragskanal 11.5 and discharged via a Grobgutaustragsschacht from the tube mill.
- Fig. 4 shows a tube mill with a first grinding chamber 1, a second grinding chamber 2 and arranged between two grinding chambers, mitrotierenden intermediate wall 3.
- a classifying device is provided, for example, according to one of the in the Fig. 1-3 illustrated variants may be formed.
- the inner diameter of the first grinding chamber 1 is smaller than the inner diameter of the following in the material flow direction grinding chamber 2.
- both the ground material from the first grinding chamber 1 and the ground material from the second passes Grinding chamber 2 in a co-rotating intermediate wall 13 arranged between the two grinding chambers.
- the intermediate wall 13 in turn contains a classifying device 13.2, which may be designed, for example, according to one of the variants indicated above. In the illustrated embodiment, it is formed by a sieve wall.
- the classifier 13.2 again separates the intermediate wall into a first intermediate wall region 13.1 and a second intermediate wall region 13.3.
- the intermediate wall 13 is delimited to the first grinding chamber 1 via a slot wall 13.4 and the second grinding chamber 2 via a slot wall 13.6.
- the millbase from the first grinding chamber 1 passes through inlet openings 13.5 in the first partition wall area 13.1.
- the ground material from the second grinding chamber 2 passes through inlet openings 13.7 into the second intermediate wall region.
- the classifying device 13.2 designed as a screen wall allows the fine material to pass from the first intermediate wall region 13.1 into the second intermediate wall region 13.3.
- the coarse material 8 from the first partition wall area 13.1 is discharged separately via first discharge means 13.8.
- the fine material 9 and the material to be ground 12 from the second grinding chamber 2 are discharged via second discharge means 13.9 from the tube mill.
- the material discharged from the second intermediate wall region 13.3 is preferably fed to a separator 16.
- the material is there divided into finished product 15 and classifier 14, wherein the classifier, preferably on a Mahlgutiergabe 17 of the second grinding chamber 2, are returned to the grinding process again.
- a tube mill which consist essentially of a first grinding chamber 1, a second grinding chamber 2, and arranged between the grinding chambers, co-rotating intermediate wall 30.
- a separating device 32 for dividing the ground material from the first grinding chamber 1 in a first Mahlgutteilmenge 8 and a second Mahlgutteilmenge 9 is provided.
- the separating device is preferably designed as a classifying unit, can in this area only a quantitative distribution can be made. In this way, two or three streams of material can be led out separately from the tube mill, resulting in advantages for the procedural material management.
- the residence time in the two grinding chambers can be influenced and controlled and, if appropriate, used to optimize the working requirement.
- Fig. 6-12 shown tube mills can in particular according to one of Fig. 1-5 be described embodiments described.
- a tube mill is operated in the closed grinding circuit with a classifier 40.
- the ground material of the first grinding chamber 1 enters the intermediate wall 30 and is divided there into a first Mahlgutteilmenge 8 and a second Mahlgutteilmenge 9. While the first Mahlgutteilmenge 8 is discharged from the tube mill, passes the second Mahlgutteilmenge 9 in the second grinding chamber 2.
- the discharged from the second grinding chamber 2 Good 18 is given to a classifier 40, which can be formed by a static or dynamic separator or classifier.
- the fine material of the classifying apparatus is discharged as finished product 19, while the coarse material 20 is transported via a material divider 41 partly or completely into the second grinding chamber 2 or into the first grinding chamber 1.
- the first grinding chamber 1 is also supplied with the first millbase subset 8 and the fresh material 21.
- first Mahlgutteilmenge 8 is fed to a classifier 50.
- the first Mahlgutteilmenge 8 is thus classified outside the tube mill, wherein the coarse material portion of the first grinding chamber 1 is abandoned.
- the fines of the classifying apparatus 50 can be fed via a material divider 51 completely or partly to the second grinding chamber 2 or the classifying apparatus 40.
- Fig. 8 The tube mill is operated in a closed grinding circuit with a classifier 40 and a Vorzerkleinticiansshake.
- the fresh product 21 is fed to a grinding unit 60, which pre-shreds the Malgut.
- the entire or a part of the pre-shredded material is then the first grinding chamber 1 abandoned.
- a material divider 61 makes it possible to recirculate part of the pre-shredded material back to the grinding unit 60.
- the discharged from the tube mill first Mahlgutteilmenge can be supplied via a splitter 52 completely or only part of the first grinding chamber 1 or the grinding unit 60.
- Fig. 9 shows the variant according to Fig. 7 in conjunction with a grinding unit 60 according to Fig. 8 ,
- the coarse material of the classifying apparatus 50 can thereby be given up completely or partly to the first grinding chamber 1 or the grinding unit 60.
- the grinding plant according to Fig. 10 provides a pre-crushing stage with a milling unit 60 in conjunction with a classifier 62.
- the classifying apparatus can be designed as a static or dynamic classifier.
- the discharged from the tube mill first Mahlgutteilmenge 8 can be supplied via a material divider 53 in part or completely the first grinding chamber 1, the classifying apparatus 62 or the classifying apparatus 40.
- the fines of the classifying apparatus 62 are supplied via a material divider 64 either completely or partly to the second grinding chamber 2 or the first grinding chamber 1.
- the coarse material of the classifying apparatus 62 passes via a material divider 63 either completely or partially into the first grinding chamber 1 and / or to the grinding unit 60, which is thus operated on the one hand with fresh material 21 and on the other with coarse material from the classifying apparatus 62.
- the coarse material of the grinding unit 60 then passes into the Classifying apparatus 62. There is also the possibility of giving up fresh goods 22, bypassing the pre-shredding, directly to the first painting chamber.
- the grinding plants according to Fig. 11 and 12 use tube mills with a center discharge.
- the first Mahlgutteilmenge 8 is discharged separately.
- the second Mahlgutteilmenge 9 is discharged together with the entering from the second grinding chamber 2 in the intermediate wall material to be ground 23 and the classifying machine 40 abandoned.
- the coarse material of the classifier 40 is partially or completely abandoned via a material divider 41 of the second grinding chamber 2. Another part can be returned to the first grinding chamber 1.
- the first Mahlgutteilmenge 8 is supplied via a material divider 53 partially or completely the first grinding chamber 1, the classifier 40 or the classifier 62.
- the variant according to Fig. 12 differs from the grinding plant according to Fig. 11 in that the second millbase subset 9 and the millbase 23 entering the intermediate wall 2 are discharged separately from one another, so that three material streams, namely the first millbase subset 8, the second millbase subset 9 and the mill base 23, are discharged from the tube mill.
- the first Mahlgutteilmenge 8 is supplied as before a material divider 53.
- the material to be ground 23 from the second grinding chamber passes directly into the classifying apparatus 40 while the second Mahlgutteilmenge 9 via a material divider 54 partially or completely the second grinding chamber 2 and / or the classifying machine 40 is abandoned.
Landscapes
- Engineering & Computer Science (AREA)
- Food Science & Technology (AREA)
- Crushing And Grinding (AREA)
- Combined Means For Separation Of Solids (AREA)
Description
Die Erfindung betrifft eine Rohrmühle sowie ein Verfahren zur Zerkleinerung von stückigem Mahlgut.The invention relates to a tube mill and a method for crushing lumpy material.
Rohrmühlen, insbesondere Kugelmühlen, sind hinlänglich bekannt. Sie bestehen im Wesentlichen aus einer ersten Mahlkammer, wenigstens einer zweiten Mahlkammer sowie einer zwischen den Mahlkammern angeordneten, mitrotierenden Zwischenwand. Sie werden zur Zerkleinerung unterschiedlicher Materialien in den verschiedensten Industriebereichen eingesetzt.Tube mills, in particular ball mills, are well known. They essentially consist of a first grinding chamber, at least one second grinding chamber and a co-rotating intermediate wall arranged between the grinding chambers. They are used for shredding different materials in various industrial sectors.
Das zu zerkleinernde Material wird beim Mahlprozess von der freibeweglichen Mahlkörperschüttung im Inneren der Mahlkammer zerkleinert, wobei als Mahlkörper sowohl kugelförmige als auch stangen- oder stangenabschnittsartige Körper verwendet werden.The material to be crushed is comminuted during the grinding process of the freely movable Mahlkörperschüttung inside the grinding chamber, being used as a grinding body both spherical and rod or rod-like body.
Durch die Verwendung von getrennten Mahlkammern ist der effektive Einsatz von Mahlkörpern mit unterschiedlicher geometrischer Ausbildung, insbesondere der Einsatz unterschiedlicher Durchmesser bei kugelförmigen Mahlkörpern, möglich. Die einzelnen Mahlkammern können auch unterschiedliche Mahlkörperfüllungsgrade aufweisen.By using separate grinding chambers, the effective use of grinding media with different geometric design, in particular the use of different diameters in spherical grinding media, is possible. The individual grinding chambers can also have different Mahlkörperfüllungsgrade.
Die Zwischenwände in den Rohrmühlen dienen dem Zweck, die Mahlkörperfüllung benachbarter Mahlkammern voneinander zu trennen und das Mahlgut kontrolliert von der einen in die andere Mahlkammer zu transportieren. Hierzu ist in der Zwischenwand üblicherweise eine Austragseinrichtung angeordnet, durch die das über Eintragsöffnungen in die Zwischenkammer gelangte Mahlgut über eine Austragsöffnung in die zweite Mahlkammer ausgetragen wird.The intermediate walls in the tube mills serve the purpose of separating the grinding media filling of adjacent grinding chambers from one another and to transport the material being ground in a controlled manner from one to the other grinding chamber. For this purpose, a discharge device is usually arranged in the intermediate wall, through which the grist received via entry openings into the intermediate chamber is discharged via a discharge opening into the second grinding chamber.
Um die Effizienz der Rohrmühle zu steigern, ist es bereits bekannt, dass aus der ersten Mahlkammer in die Zwischenwand eintretende Mahlgut in Grobgut und Feingut zu trennen, wobei das Feingut über eine Austragsöffnung in die zweite Mahlkammer gelangt und das Grobgut über einen Austragskonus direkt hinter die Zwischenwand in die erste Mahlkammer zurückgeworfen wird.To increase the efficiency of the tube mill, it is already known that from the first grinding chamber in the intermediate wall entering grinding material in coarse material and fine material to separate, wherein the fine material passes through a discharge opening into the second grinding chamber and the coarse material is thrown back via a discharge cone directly behind the partition into the first grinding chamber.
In der
In der
Aus der
Der Erfindung liegt nun die Aufgabe zugrunde, den Wirkungsgrad einer Rohrmühle sowie eines Verfahrens zum Zerkleinern von stückigem Mahlgut zu verbessern.The invention is based on the object to improve the efficiency of a tube mill and a method for crushing lumpy material to be ground.
Erfindungsgemäß wird diese Aufgabe durch die Merkmale der Ansprüche 1 und 10 gelöst.According to the invention, this object is solved by the features of
Weitere Ausgestaltungen der Erfindung sind Gegenstand der Unteransprüche.Further embodiments of the invention are the subject of the dependent claims.
Die erfindungsgemäße Rohrmühle besteht im Wesentlichen aus
- a. einer ersten Mahlkammer,
- b. wenigstens einer zweiten Mahlkammer,
- c. einer zwischen den Mahlkammern angeordneten, mitrotierenden Zwischenwand,
- d. einer in der Zwischenwand angeordneten Trenneinrichtung zum Aufteilen des Mahlguts aus der ersten Mahlkammer in eine erste Mahlgutteilmenge und eine zweite Mahlgutteilmenge,
- e. Mitteln zum direkten oder indirekten Zuführen wenigstens eines Teils der zweiten Mahlgutteilmenge zur zweiten Mahlkammer sowie
- f. eine Einrichtung zum separaten Ausschleusen der ersten Mahlgutteilmenge aus der Rohrmühle.
- a. a first grinding chamber,
- b. at least a second grinding chamber,
- c. a co-rotating intermediate wall arranged between the grinding chambers,
- d. a separation device arranged in the intermediate wall for dividing the ground material from the first grinding chamber into a first Mahlgutteilmenge and a second Mahlgutteilmenge,
- e. Means for direct or indirect feeding at least a portion of the second Mahlgutteilmenge to the second grinding chamber and
- f. a device for separate discharge of the first Mahlgutteilmenge from the tube mill.
Beim erfindungsgemäßen Verfahren zum Zerkleinern von stückigem Mahlgut mit einer Rohrmühle, enthaltend wenigstens eine erste und eine zweite Mahlkammer sowie eine zwischen den Mahlkammern angeordnete, mitrotierende Zwischenwand, wird das in der ersten Mahlkammer zerkleinerte Mahlgut in einer Zwischenwand in eine erste und eine zweite Mahlgutteilmenge aufgeteilt, wobei zumindest ein Teil der zweiten Mahlgutteilmenge direkt oder indirekt in die zweite Mahlkammer gelangt und zumindest die erste Mahlgutteilmenge separat aus der Rohrmühle ausgeschleust wird.In the inventive method for crushing lumpy material to be ground with a tube mill containing at least a first and a second grinding chamber and a co-rotating between the grinding chambers, mitrotierende intermediate wall, the comminuted in the first grinding chamber millbase is divided in an intermediate wall in a first and a second Mahlgutteilmenge, wherein at least a portion of the second Mahlgutteilmenge passes directly or indirectly into the second grinding chamber and at least the first Mahlgutteilmenge is discharged separately from the tube mill.
Erfindungsgemäß wird die Trenneinrichtung durch eine Klassiereinrichtung gebildet, so dass die erste Mahlgutteilmenge aus Grobgut und die zweite Mahlgutteilmenge aus Feingut besteht. Die Klassiereinrichtung kann beispielsweise durch eine Sieb- bzw. Schlitzwand, ein Trommelsieb oder Siebhubschaufeln gebildet werden. Die ausgeschleuste erste Mahlgutteilmenge kann ganz oder teilweise der Mahlgutaufgabe der ersten Mahlkammer oder einem Vormahlaggregat zugeführt werden.According to the invention the separating device is formed by a classifying device, so that the first Mahlgutteilmenge consists of coarse material and the second Mahlgutteilmenge consists of fine material. The classifier can be formed, for example, by a sieve or trench wall, a drum screen or Siebhubschaufeln. The discharged first Mahlgutteilmenge can be wholly or partially fed to the Mahlgutaufgabe the first grinding chamber or a Vormahlaggregat.
Weitere Vorteile und Ausgestaltungen der Erfindung werden im Folgenden anhand der Beschreibung einige Ausführungsbeispiele und der Zeichnung näher erläutert.Further advantages and embodiments of the invention will be explained in more detail below with reference to the description of some embodiments and the drawings.
- Fig. 1a - Fig. 1cFig. 1a - Fig. 1c
- schematische Darstellungen einer Rohrmühle gemäss einem ersten Ausführungsbeispiel,schematic representations of a tube mill according to a first embodiment,
- Fig. 2a - Fig. 2eFig. 2a - Fig. 2e
- schematische Darstellungen einer Rohrmühle gemäss einem zweiten Ausführungsbeispiel,schematic representations of a tube mill according to a second embodiment,
- Fig. 3a - Fig. 3bFig. 3a - Fig. 3b
- schematische Darstellungen einer Rohrmühle gemäss einem dritten Ausführungsbeispiel,schematic representations of a tube mill according to a third embodiment,
- Fig. 4Fig. 4
- schematische Darstellungen einer Rohrmühle gemäss einem vierten Ausführungsbeispiel,schematic representations of a tube mill according to a fourth embodiment,
- Fig. 5a - Fig. 5bFig. 5a - Fig. 5b
- schematische Darstellungen einer Rohrmühle gemäss einem fünften Ausführungsbeispiel,schematic representations of a tube mill according to a fifth embodiment,
- Fig. 6 - Fig. 12Fig. 6 - Fig. 12
- schematische Darstellungen von Mahlanlagen mit einer erfindungsgemäßen Rohrmühle gemäss verschiedener Varianten.schematic representations of grinding plants with a tube mill according to the invention according to various variants.
Die in
Die erste Mahlkammer ist von der Zwischenwand 3 üblicherweise durch eine Schlitzwand 3.4 getrennt, die Öffnungen 3.5 aufweist, durch die das in der ersten Mahlkammer genügend zerkleinerte Mahlgut in einen ersten Zwischenwandbereich 3.1 gelangt.The first grinding chamber is usually separated from the
Die Zwischenwand 3 weist neben dem ersten Zwischenwandbereich 3.1 einen zweiten Zwischenwand 3.3 auf, wobei die beiden Zwischenwandbereiche durch eine Klassiereinrichtung 3.2 voneinander getrennt sind. Die integrierte Klassiereinrichtung 3.2 teilt das Mahlgut aus der ersten Mahlkammer in eine aus Grobgut 8 bestehende erste Mahlgutteilmenge und eine aus Feingut 9 bestehende zweite Mahlgutteilmenge auf. Das Feingut 9 gelangt dabei in den zweiten Zwischenwandbereich 3.3 und wird dort über geeignete Mittel, beispielsweise Hubelemente, der zweiten Mahlkammer 2 zugeführt. Das innerhalb der Klassiereinrichtung 3.2 anfallende Grobgut 8 wird aus der Rohrmühle ausgeschleust und kann an geeigneter Stelle (vorzugsweise am Mahlguteinlauf 4) wieder dem Mahlprozess zugeführt werden.The
Im Folgenden wird der Aufbau und die Funktionsweise der Zwischenwand 3 anhand der
Im dargestellten Ausführungsbeispiel ist die Klassiereinrichtung 3.2 als Sieb- bzw. Schlitzwand ausgebildet. Der erste Zwischenwandbereich 3.1 wird dabei von der Schlitzwand 3.4 sowie der Klassiereinrichtung 3.2 und der zweite Zwischenwandbereich 3.3 durch die Klassiereinrichtung 3.2 und eine die Zwischenwand 3 von der zweiten Mahlkammer 2 trennende Stirnwand 3.6 begrenzt.In the illustrated embodiment, the classifying device 3.2 is designed as a screen or diaphragm wall. The first partition wall area 3.1 is thereby bounded by the slot wall 3.4 and the classifying device 3.2 and the second partition wall area 3.3 by the classifying device 3.2 and the
Das aus der ersten Mahlkammer 1 über die Öffnung 3.5 in den ersten Zwischenwandbereich 3.1 kommende Feingut 9 gelangt ungehindert über die Klassiereinrichtung 3.2 in den zweiten Zwischenwandbereich 3.3 und wird dort über eine nicht näher dargestellte Austragseinrichtung (insbesondere Hubschaufeln) in die zweite Mahlkammer 2 ausgetragen.The
Das aus der ersten Mahlkammer 1 in den ersten Zwischenwandbereich 3.1 eingetragene Grobgut 8 verbleibt vor der Klassiereinrichtung 3.2, wobei der Grobgutspiegel im ersten Zwischenwandbereich allmählich steigt, bis er eine bestimmte Höhe erreicht hat, bei der das Grobgut 8 über eine konstruktiv vorgesehene Austragsöffnung 3.10 in eine innerhalb der Klassiereinrichtung 3.2 angeordnete Austragseinrichtung 3.8 gelangt. Über einen Austrittskanal 3.9 wird das Grobgut 8 durch ein Austragsgehäuse 3.11 aus der Rohrmühle ausgeschleust.The
Je nach verfahrenstechnischen Anforderungen und Erfordernissen kann die Höhe des Pegels des Grobguts 8 vor der Klassiereinrichtung 3.2 durch Variation des radialen Abstands der Austragsöffnung 3.10 von der Längsmittelachse 6 eingestellt werden. Die Menge des ausgeschleusten Grobgut 8 kann durch Variation der Größe der Austragsöffnung 3.10 eingestellt werden.Depending on the procedural requirements and requirements, the height of the level of the
In
Die Zwischenwand 10 ist in mindestens eine, vorzugsweise, aber mehrere Siebkammem aufgeteilt, die segmentartig um die Längsmittelachse 6 angeordnet sind. Jede Siebkammer wird durch radiale Seitenwände 10.9, 10.10 sowie einen Teil der zur ersten Mahlkammer 1 weisenden Schlitzwand 10.4 sowie einen Teil der zur zweiten Mahlkammer 2 weisenden Stirnwand 10.6 begrenzt.
Die in den
Das Mahlgut gelangt über Eintrittsöffnungen in der Schlitzwand 11.4 in den ersten Zwischenwandbereich der Siebtrommel 11.2. Auf dem Weg zum Grobgutaustragskanal 11.5, der am Ende der Siebtrommel angeordnet ist, fällt das Feingut 9 durch die Siebtrommel in den zweiten Zwischenwandbereich 11.3. Über Förderbleche 11.6, die vorzugsweise als Schneckenbleche ausgebildet sind, wird das Feingut 9 in die zweite Mahlkammer 2 gefördert. Das Grobgut 8 wird im Grobgutaustragskanal 11.5 gesammelt und über einen Grobgutaustragsschacht aus der Rohrmühle ausgeschleust.The ground material passes through inlet openings in the slot wall 11.4 in the first intermediate wall region of the screen drum 11.2. On the way to Grobgutaustragskanal 11.5, which is arranged at the end of the sieve drum, the
Das Ausführungsbeispiel gemäss
Der Innendurchmesser der ersten Mahlkammer 1 ist dabei kleiner als der Innendurchmesser der in Materialflussrichtung folgenden Mahlkammer 2. Durch einen solchen Stufensprung kann eine optimierte Geometrie erzeugt werden, die dem Mahlkörperfüllungsgrad, den Mahlkörperabmessungen, der Art des Mahlguts usw. Rechnung trägt.The inner diameter of the first grinding
Während bei allen bisher gezeigten Varianten das Feingut direkt über eine die Zwischenwand von der zweiten Mahlgutkammer trennende Stirnwand in die zweite Mahlkammer gelangt, ist im Ausführungsbeispiel gemäss
Die Zwischenwand 13 wird zur ersten Mahlkammer 1 über eine Schlitzwand 13.4 und zur zweiten Mahlkammer 2 über eine Schlitzwand 13.6 abgegrenzt. Das Mahlgut aus der ersten Mahlkammer 1 tritt über Eintrittsöffnungen 13.5 in den ersten Zwischenwandbereich 13.1. Das Mahlgut aus der zweiten Mahlkammer 2 gelangt über Eintrittsöffnungen 13.7 in den zweiten Zwischenwandbereich. Die als Siebwand ausgebildete Klassiereinrichtung 13.2 lässt das Feingut aus dem ersten Zwischenwandbereich 13.1 in den zweiten Zwischenwandbereich 13.3 passieren.The
Das Grobgut 8 aus dem ersten Zwischenwandbereich 13.1 wird über erste Austragsmittel 13.8 separat ausgeschleust. Das Feingut 9 und das Mahlgut 12 aus der zweiten Mahlkammer 2 werden über zweite Austragsmittel 13.9 aus der Rohrmühle ausgetragen. Gemäss
Im Folgenden werden verschiedene Mahlanlagen beschrieben, die jeweils eine Rohrmühle aufweisen, die im Wesentlichen aus einer ersten Mahlkammer 1, einer zweiten Mahlkammer 2, und einer zwischen den Mahlkammern angeordneten, mitrotierenden Zwischenwand 30 bestehen. In der Zwischenwand ist ein Trenneinrichtung 32 zum Aufteilen des Mahlguts aus der ersten Mahlkammer 1 in eine erste Mahlgutteilmenge 8 und eine zweite Mahlgutteilmenge 9 vorgesehen. Wenngleich die Trenneinrichtung vorzugsweise als Klassiereinheit ausgebildet, kann in diesem Bereich auch lediglich eine mengenmäßige Aufteilung vorgenommen werden. Auf diese Weise können aus der Rohrmühle zwei bzw. drei Materialströme separat herausgeführt werden, wodurch sich Vorteile für die verfahrenstechnische Materialführung ergeben. So kann insbesondere die Verweilzeit in den beiden Mahlkammern beeinflusst und kontrolliert werden und gegebenenfalls zur Optimierung des Arbeitsbedarfes verwendet werden.In the following, various grinding plants are described, each having a tube mill, which consist essentially of a first
Die in den
In
Die in
In
Die aus der Rohrmühle ausgeschleuste erste Mahlgutteilmenge kann über einen Splitter 52 vollständig oder nur zu einem Teil der ersten Mahlkammer 1 oder dem Mahlaggregat 60 zugeführt werden.The discharged from the tube mill first Mahlgutteilmenge can be supplied via a
Die Mahlanlage gemäss
Die aus der Rohrmühle ausgeschleuste erste Mahlgutteilmenge 8 kann über einen Materialteiler 53 zum Teil oder vollständig der ersten Mahlkammer 1, dem Klassierapparat 62 oder dem Klassierapparat 40 zugeführt werden. Das Feingut des Klassierapparates 62 wird über einen Materialteiler 64 entweder vollständig oder zum Teil der zweiten Mahlkammer 2 oder der ersten Mahlkammer 1 zugeführt. Das Grobgut des Klassierapparates 62 gelangt über einen Materialteiler 63 entweder vollständig oder zum Teil in die erste Mahlkammer 1 und/oder zum Mahlaggregat 60, welches somit zum einen mit Frischgut 21 und zum anderen mit Grobgut aus dem Klassierapparat 62 betrieben wird. Das Grobgut des Mahlaggregat 60 gelangt dann in den Klassierapparat 62. Es besteht außerdem die Möglichkeit Frischgut 22 unter Umgehung der Vorzerkleinerung direkt der ersten Malkammer aufzugeben.The discharged from the tube mill first Mahlgutteilmenge 8 can be supplied via a
Die Mahlanlagen gemäss
Die Variante gemäss
Die oben aufgezeigten Varianten von Mahlanlagen sind lediglich beispielhaft zu verstehen. Sie zeigen jedoch, dass die ausgeschleuste erste Mahlgutteilmenge auf vielfältige Weise vor- bzw. nachgeschalteten Anlagenteilen zugeführt werden kann. Dadurch wird eine bessere Mahleffizienz und Vorteile in der Materialführung ermöglicht, wodurch der spezifische Arbeitsbedarf verringert werden kann.The above-mentioned variants of grinding plants are to be understood as exemplary only. However, they show that the discharged first Mahlgutteilmenge can be supplied in a variety of ways upstream or downstream equipment parts. This allows better grinding efficiency and material handling advantages, which can reduce specific workload.
Claims (18)
- A tube mill comprisinga. a first grinding chamber (1),b. at least one second grinding chamber (2),c. a jointly rotating partition (3) arranged between the grinding chambers,d. a classifier (3.2), arranged in the partition, for dividing the grinding material from the first grinding chamber into a first grinding-material quantity (8) and a second grinding-material quantity (9),e. means for supplying at least some of the second grinding-material quantity to the second grinding chamber,f. a device (3.8) for separately discharging the first grinding-material quantity from the tube mill,characterised in that the classifier (3.2) is formed so that the first grinding-material quantity consists of coarse material and the second grinding-material quantity consists of fine material.
- A tube mill according to claim 1, characterised by means for supplying the discharged first grinding-material quantity to the grinding-material feeder (5) of the first grinding chamber.
- A tube mill according to claim 1, characterised in that the means for supplying the second grinding-material quantity to the second grinding chamber (2) are arranged so that the second grinding-material quantity (9) passes into the second grinding chamber (2) via an end wall (3.6) separating the partition from the second grinding chamber.
- A tube mill according to claim 1, characterised in that the partition has a first and a second partition region (3.1, 3.3), wherein the two partition regions are separated from one another by the separator (3.2), and the device for discharging the first grinding-material quantity from the tube mill communicates with the first partition region and the means for supplying the second grinding-material quantity to the second grinding chamber communicate with the second partition region.
- A tube mill according to claim 1, characterised in that the inner diameter of the first grinding chamber (1) is smaller than the inner diameter of the second grinding chamber (2).
- A tube mill according to claim 1, characterised in that the separator is formed by a screening or slotted wall (3.2).
- A tube mill according to claim 1, characterised in that the separator is formed by a screening drum (11.2).
- A tube mill according to claim 1, characterised in that the separator is formed by lifting vanes provided in the partition, wherein the lifting vanes are formed as screening lifting vanes (10.2).
- A tube mill according to claim 1, characterised by means (13.7) for transferring the grinding material from the second grinding chamber (2) to the partition (13) and means (13.9) for discharging the material coming from the second grinding chamber and for discharging the second grinding-material quantity from the tube mill.
- A method of comminuting lumpy grinding material in a tube mill, containing at least one first and one second grinding chamber (1, 2) and a jointly rotating partition (30) arranged between the grinding chambers, wherein the grinding material ground in the first grinding chamber is classified in the partition and divided into a first and a second grinding-material quantity (8, 9), wherein the one grinding-material quantity (8) consists of coarse material and the other (9) consists of fine material, and wherein at least some of the second grinding-material quantity (9) passes into the second grinding chamber (2) and at least the first grinding-material quantity (8) is discharged separately from the tube mill, characterised in that the first grinding-material quantity (8) is formed by the coarse material and the second grinding-material quantity (9) is formed by the fine material.
- A method according to claim 10, characterised in that at least some of the discharged first grinding-material quantity (8) is fed back to the grinding-material feeder of the first grinding chamber (1).
- A method according to claim 10, characterised in that one part of the discharged first grinding-material quantity (8) is fed back to the grinding-material feeder of the first grinding chamber (1) and the other part is fed back to a classifying apparatus (40) arranged outside the tube mill.
- A method according to claim 10, characterised in that the discharged first grinding-material quantity (8) is fed back to a classifying apparatus (40, 62) arranged outside the tube mill.
- A method according to claim 10, characterised in that the grinding material ground in the second grinding chamber (2) is fed to a classifying apparatus (40) arranged outside the tube mill, wherein the coarse material (20) accumulating therein is fed back to the second grinding chamber (2) and/or to the first grinding chamber (1).
- A method according to claim 10, characterised in that the grinding material to be supplied to the tube mill is first fed to a precomminuting stage (60).
- A method according to claim 10, characterised in that the grinding material to be supplied to the tube mill is first fed to a precomminuting stage and in that one part of the discharged first grinding-material quantity (8) is fed to the precomminuting stage again, while the other part is conveyed to the grinding-material feeder of the first grinding chamber.
- A method according to claim 10, characterised in that the grinding material to be supplied to the tube mill is first fed to a precomminuting stage (60) and some of the precomminuted material is recirculated to the precomminuting stage.
- A method according to claim 10, characterised in that the grinding material to be supplied to the tube mill is first fed to a precomminuting stage (60) and the precomminuted material is supplied to a classifying apparatus (62) arranged downstream, the coarse material from which is conducted to the first grinding chamber (1) and/or to the precomminuting stage (60) and the fine material from which passes to the second grinding chamber (2).
Applications Claiming Priority (3)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE10158710 | 2001-11-29 | ||
DE10158710 | 2001-11-29 | ||
PCT/EP2002/013461 WO2003045563A1 (en) | 2001-11-29 | 2002-11-28 | Tube grinder and method for comminuting lumpy grinding stock |
Publications (2)
Publication Number | Publication Date |
---|---|
EP1448303A1 EP1448303A1 (en) | 2004-08-25 |
EP1448303B1 true EP1448303B1 (en) | 2008-08-27 |
Family
ID=7707469
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP02787865A Expired - Lifetime EP1448303B1 (en) | 2001-11-29 | 2002-11-28 | Tube grinder and method for comminuting lumpy grinding stock |
Country Status (6)
Country | Link |
---|---|
US (1) | US7073737B2 (en) |
EP (1) | EP1448303B1 (en) |
AU (1) | AU2002352181A1 (en) |
DE (1) | DE50212715D1 (en) |
DK (1) | DK1448303T3 (en) |
WO (1) | WO2003045563A1 (en) |
Families Citing this family (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE102004045959A1 (en) * | 2004-09-22 | 2006-03-23 | Polysius Ag | Mill material milling system, has rough mill area that is formed in such a manner that less than twenty five percent of applied driving power of pipe mill is transferred within rough mill area |
DE102005007254A1 (en) * | 2005-02-16 | 2006-08-17 | Polysius Ag | Grinding plant and process for grinding regrind |
DE102010017394A1 (en) * | 2010-06-16 | 2011-12-22 | Polysius Ag | Process for comminuting regrind by means of a tube mill |
JP5825646B2 (en) * | 2011-03-31 | 2015-12-02 | 有限会社大東土木 | Grinder |
US20160030944A1 (en) * | 2014-08-04 | 2016-02-04 | General Electric Company | Attritor |
CN113731562B (en) * | 2021-06-25 | 2022-12-06 | 浙江交投矿业有限公司 | Wet processing technology for tuff macadam |
Family Cites Families (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE378026C (en) | 1923-07-04 | Clemens Redeligx | Milling process with step-by-step comminution of the material to be ground in the pre-grinding and fine grinding chambers arranged in a grinding housing, but separated from one another | |
US1504777A (en) * | 1921-04-07 | 1924-08-12 | Allis Chalmers Mfg Co | Comminuting mill |
US1748920A (en) * | 1928-02-23 | 1930-02-25 | Allis Chalmers Mfg Co | Process of and apparatus for comminuting material |
DE1507650C3 (en) * | 1965-05-04 | 1973-10-04 | F. L. Smidth & Co. A/S, Kopenhagen | Grinding sludge drum |
BE711701A (en) * | 1968-03-05 | 1968-07-15 | ||
GB2038202B (en) * | 1978-12-29 | 1982-12-01 | Smidth & Co As F L | Dry grinding a granular material |
DE19512509B4 (en) * | 1995-04-04 | 2009-07-30 | Polysius Ag | Process for comminuting ore material |
US6180040B1 (en) | 1998-09-02 | 2001-01-30 | Acushnet Company | Method of forming a golf ball core |
-
2002
- 2002-11-28 DE DE50212715T patent/DE50212715D1/en not_active Expired - Lifetime
- 2002-11-28 DK DK02787865T patent/DK1448303T3/en active
- 2002-11-28 AU AU2002352181A patent/AU2002352181A1/en not_active Abandoned
- 2002-11-28 WO PCT/EP2002/013461 patent/WO2003045563A1/en active IP Right Grant
- 2002-11-28 US US10/497,293 patent/US7073737B2/en not_active Expired - Lifetime
- 2002-11-28 EP EP02787865A patent/EP1448303B1/en not_active Expired - Lifetime
Also Published As
Publication number | Publication date |
---|---|
EP1448303A1 (en) | 2004-08-25 |
DK1448303T3 (en) | 2009-01-12 |
AU2002352181A1 (en) | 2003-06-10 |
WO2003045563A1 (en) | 2003-06-05 |
DE50212715D1 (en) | 2008-10-09 |
US7073737B2 (en) | 2006-07-11 |
US20050029374A1 (en) | 2005-02-10 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
EP0525423B1 (en) | Method and device for grinding materials of different sizes | |
EP0603481B1 (en) | Method and arrangement for milling grinding stock | |
DE69212707T2 (en) | Device for shredding used vehicle tires and the like and separating metal parts from non-metal parts from this shredded material | |
EP0460490B1 (en) | Air classifier | |
EP3154701B1 (en) | Grinding system and method for comminution of grinding stock | |
EP2191901A2 (en) | Pulveriser and method for operating same | |
EP0406591B1 (en) | Method and arrangement for milling material to be milled | |
DE102013021756A1 (en) | Mahlkörpermühle and operating method for it | |
EP0447669A1 (en) | Process and plant for two-stage grinding of brittle materials | |
EP1448303B1 (en) | Tube grinder and method for comminuting lumpy grinding stock | |
EP1332034A1 (en) | Ring extruder feed | |
EP1640070B1 (en) | Apparatus and method for grinding material | |
EP0237641B1 (en) | Comminuting plant for brittle material | |
EP1786573A1 (en) | Apparatus for classifying charge material | |
EP2054156B1 (en) | Roller mill | |
DE3710602C2 (en) | ||
DE10147591B4 (en) | grinding plant | |
DE4307230A1 (en) | Process and plant for comminuting the bed of brittle regrind | |
DE3138259C2 (en) | ||
DE102012109645A1 (en) | Separator for separating granular goods e.g. lime stone, in grinding mill, has ventilating base for separating areas, course good outlets connected to respective separating areas and fine good outlet formed in one of areas | |
EP3613508A1 (en) | Method and device for discharging poorly grindable particles from a spiral jet mill | |
DE2040663A1 (en) | Mill | |
DE19832769C2 (en) | Method for operating an agitator mill | |
DE102007020267B4 (en) | Device for separating a loose mixture in a fluid medium | |
DE2814778A1 (en) | Vertical drum loose material crusher - has two cutter discs with cutting edges forming closed zigzag shape |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
PUAI | Public reference made under article 153(3) epc to a published international application that has entered the european phase |
Free format text: ORIGINAL CODE: 0009012 |
|
17P | Request for examination filed |
Effective date: 20040526 |
|
AK | Designated contracting states |
Kind code of ref document: A1 Designated state(s): AT BE BG CH CY CZ DE DK EE ES FI FR GB GR IE IT LI LU MC NL PT SE SK TR |
|
AX | Request for extension of the european patent |
Extension state: AL LT LV MK RO SI |
|
RIN1 | Information on inventor provided before grant (corrected) |
Inventor name: ALKER, HEINZ Inventor name: KOENNING, LUDWIG Inventor name: SCHNATZ, ROBERT Inventor name: RUETHER, THOMAS Inventor name: REIMERS, JENS Inventor name: SCHULTE, LUDGER Inventor name: EICKHOLT, HUBERT Inventor name: DILLY, DIRK Inventor name: UNGETHUEM, FRANK Inventor name: GIESEMANN, REINHARD |
|
GRAP | Despatch of communication of intention to grant a patent |
Free format text: ORIGINAL CODE: EPIDOSNIGR1 |
|
GRAS | Grant fee paid |
Free format text: ORIGINAL CODE: EPIDOSNIGR3 |
|
GRAA | (expected) grant |
Free format text: ORIGINAL CODE: 0009210 |
|
AK | Designated contracting states |
Kind code of ref document: B1 Designated state(s): DE DK FR |
|
REF | Corresponds to: |
Ref document number: 50212715 Country of ref document: DE Date of ref document: 20081009 Kind code of ref document: P |
|
REG | Reference to a national code |
Ref country code: DK Ref legal event code: T3 |
|
PLBE | No opposition filed within time limit |
Free format text: ORIGINAL CODE: 0009261 |
|
STAA | Information on the status of an ep patent application or granted ep patent |
Free format text: STATUS: NO OPPOSITION FILED WITHIN TIME LIMIT |
|
26N | No opposition filed |
Effective date: 20090528 |
|
REG | Reference to a national code |
Ref country code: DE Ref legal event code: R082 Ref document number: 50212715 Country of ref document: DE Representative=s name: RA U. PA VOLKMAR TETZNER; PA MICHAEL TETZNER; , DE |
|
REG | Reference to a national code |
Ref country code: DE Ref legal event code: R081 Ref document number: 50212715 Country of ref document: DE Owner name: THYSSENKRUPP RESOURCE TECHNOLOGIES AG, DE Free format text: FORMER OWNER: POLYSIUS AG, 59269 BECKUM, DE Effective date: 20120118 Ref country code: DE Ref legal event code: R082 Ref document number: 50212715 Country of ref document: DE Representative=s name: RECHTSANW. UND PAT.-ANW. DR.-ING. DR.JUR. VOLK, DE Effective date: 20120118 Ref country code: DE Ref legal event code: R081 Ref document number: 50212715 Country of ref document: DE Owner name: THYSSENKRUPP RESOURCE TECHNOLOGIES GMBH, DE Free format text: FORMER OWNER: POLYSIUS AG, 59269 BECKUM, DE Effective date: 20120118 Ref country code: DE Ref legal event code: R082 Ref document number: 50212715 Country of ref document: DE Representative=s name: TETZNER & PARTNER MBB PATENT- UND RECHTSANWAEL, DE Effective date: 20120118 Ref country code: DE Ref legal event code: R081 Ref document number: 50212715 Country of ref document: DE Owner name: THYSSENKRUPP INDUSTRIAL SOLUTIONS AG, DE Free format text: FORMER OWNER: POLYSIUS AG, 59269 BECKUM, DE Effective date: 20120118 |
|
REG | Reference to a national code |
Ref country code: DE Ref legal event code: R082 Ref document number: 50212715 Country of ref document: DE Representative=s name: RECHTSANW. UND PAT.-ANW. DR.-ING. DR.JUR. VOLK, DE |
|
REG | Reference to a national code |
Ref country code: DE Ref legal event code: R082 Ref document number: 50212715 Country of ref document: DE Representative=s name: RECHTSANW. UND PAT.-ANW. DR.-ING. DR.JUR. VOLK, DE Effective date: 20130808 Ref country code: DE Ref legal event code: R081 Ref document number: 50212715 Country of ref document: DE Owner name: THYSSENKRUPP RESOURCE TECHNOLOGIES GMBH, DE Free format text: FORMER OWNER: THYSSENKRUPP POLYSIUS AG, 59269 BECKUM, DE Effective date: 20130626 Ref country code: DE Ref legal event code: R081 Ref document number: 50212715 Country of ref document: DE Owner name: THYSSENKRUPP RESOURCE TECHNOLOGIES GMBH, DE Free format text: FORMER OWNER: THYSSENKRUPP RESOURCE TECHNOLOGIES AG, 59269 BECKUM, DE Effective date: 20130808 Ref country code: DE Ref legal event code: R082 Ref document number: 50212715 Country of ref document: DE Representative=s name: RECHTSANW. UND PAT.-ANW. DR.-ING. DR.JUR. VOLK, DE Effective date: 20130626 Ref country code: DE Ref legal event code: R082 Ref document number: 50212715 Country of ref document: DE Representative=s name: TETZNER & PARTNER MBB PATENT- UND RECHTSANWAEL, DE Effective date: 20130626 Ref country code: DE Ref legal event code: R082 Ref document number: 50212715 Country of ref document: DE Representative=s name: TETZNER & PARTNER MBB PATENT- UND RECHTSANWAEL, DE Effective date: 20130808 Ref country code: DE Ref legal event code: R081 Ref document number: 50212715 Country of ref document: DE Owner name: THYSSENKRUPP INDUSTRIAL SOLUTIONS AG, DE Free format text: FORMER OWNER: THYSSENKRUPP POLYSIUS AG, 59269 BECKUM, DE Effective date: 20130626 Ref country code: DE Ref legal event code: R081 Ref document number: 50212715 Country of ref document: DE Owner name: THYSSENKRUPP INDUSTRIAL SOLUTIONS AG, DE Free format text: FORMER OWNER: THYSSENKRUPP RESOURCE TECHNOLOGIES AG, 59269 BECKUM, DE Effective date: 20130808 |
|
REG | Reference to a national code |
Ref country code: DE Ref legal event code: R082 Ref document number: 50212715 Country of ref document: DE Representative=s name: TETZNER & PARTNER MBB PATENT- UND RECHTSANWAEL, DE |
|
REG | Reference to a national code |
Ref country code: DE Ref legal event code: R082 Ref document number: 50212715 Country of ref document: DE Representative=s name: TETZNER & PARTNER MBB PATENT- UND RECHTSANWAEL, DE |
|
REG | Reference to a national code |
Ref country code: DE Ref legal event code: R082 Ref document number: 50212715 Country of ref document: DE Representative=s name: TETZNER & PARTNER MBB PATENT- UND RECHTSANWAEL, DE Effective date: 20140519 Ref country code: DE Ref legal event code: R081 Ref document number: 50212715 Country of ref document: DE Owner name: THYSSENKRUPP INDUSTRIAL SOLUTIONS AG, DE Free format text: FORMER OWNER: THYSSENKRUPP RESOURCE TECHNOLOGIES GMBH, 59269 BECKUM, DE Effective date: 20140729 Ref country code: DE Ref legal event code: R082 Ref document number: 50212715 Country of ref document: DE Representative=s name: TETZNER & PARTNER MBB PATENT- UND RECHTSANWAEL, DE Effective date: 20140729 |
|
REG | Reference to a national code |
Ref country code: FR Ref legal event code: PLFP Year of fee payment: 14 |
|
REG | Reference to a national code |
Ref country code: FR Ref legal event code: PLFP Year of fee payment: 15 |
|
REG | Reference to a national code |
Ref country code: FR Ref legal event code: PLFP Year of fee payment: 16 |
|
PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: DE Payment date: 20181120 Year of fee payment: 17 Ref country code: DK Payment date: 20181122 Year of fee payment: 17 |
|
PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: FR Payment date: 20181123 Year of fee payment: 17 |
|
REG | Reference to a national code |
Ref country code: DE Ref legal event code: R082 Ref document number: 50212715 Country of ref document: DE Representative=s name: TETZNER & PARTNER MBB PATENT- UND RECHTSANWAEL, DE Ref country code: DE Ref legal event code: R081 Ref document number: 50212715 Country of ref document: DE Owner name: THYSSENKRUPP INDUSTRIAL SOLUTIONS AG, DE Free format text: FORMER OWNER: THYSSENKRUPP INDUSTRIAL SOLUTIONS AG, 45143 ESSEN, DE |
|
REG | Reference to a national code |
Ref country code: DE Ref legal event code: R119 Ref document number: 50212715 Country of ref document: DE |
|
REG | Reference to a national code |
Ref country code: DK Ref legal event code: EBP Effective date: 20191130 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: DE Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20200603 Ref country code: FR Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20191130 Ref country code: DK Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20191130 |