EP2125230B1 - Procédé pour fonctionnement de broyage à sec en continu d'une tour de broyage par friction et tour de broyage par friction - Google Patents

Procédé pour fonctionnement de broyage à sec en continu d'une tour de broyage par friction et tour de broyage par friction Download PDF

Info

Publication number
EP2125230B1
EP2125230B1 EP08700982.5A EP08700982A EP2125230B1 EP 2125230 B1 EP2125230 B1 EP 2125230B1 EP 08700982 A EP08700982 A EP 08700982A EP 2125230 B1 EP2125230 B1 EP 2125230B1
Authority
EP
European Patent Office
Prior art keywords
grinding
gas
milling container
package
inlet
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.)
Not-in-force
Application number
EP08700982.5A
Other languages
German (de)
English (en)
Other versions
EP2125230A1 (fr
EP2125230B8 (fr
Inventor
Stefan Gerl
Jens Sachweh
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Maschinenfabrik Gustav Eirich GmbH and Co KG
Original Assignee
Maschinenfabrik Gustav Eirich GmbH and Co KG
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Maschinenfabrik Gustav Eirich GmbH and Co KG filed Critical Maschinenfabrik Gustav Eirich GmbH and Co KG
Priority to PL08700982T priority Critical patent/PL2125230T3/pl
Publication of EP2125230A1 publication Critical patent/EP2125230A1/fr
Publication of EP2125230B1 publication Critical patent/EP2125230B1/fr
Application granted granted Critical
Publication of EP2125230B8 publication Critical patent/EP2125230B8/fr
Not-in-force legal-status Critical Current
Anticipated expiration legal-status Critical

Links

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
    • 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
    • B02C17/16—Mills in which a fixed container houses stirring means tumbling the charge
    • 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
    • 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
    • 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
    • B02C17/186—Adding fluid, other than for crushing by fluid energy
    • B02C17/1875—Adding fluid, other than for crushing by fluid energy passing gas through crushing zone
    • B02C17/188—Adding fluid, other than for crushing by fluid energy passing gas through crushing zone characterised by point of gas entry or exit or by gas flow path
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B02—CRUSHING, PULVERISING, OR DISINTEGRATING; PREPARATORY TREATMENT OF GRAIN FOR MILLING
    • B02C—CRUSHING, PULVERISING, OR DISINTEGRATING IN GENERAL; MILLING GRAIN
    • B02C19/00—Other disintegrating devices or methods
    • B02C19/22—Crushing mills with screw-shaped crushing means

Definitions

  • the invention relates to a method for the continuous dry grinding operation of a tower friction mill according to the preamble of claim 1 and a tower friction mill according to the preamble of claim 10.
  • a generic tower friction mill is from the U.S. Patent 4,754,934 known.
  • the gas is introduced at the bottom of the grinding container and flows through the packing of grinding media and millbase.
  • a centrifuge is mounted on the drive shaft, which is intended to eject the grinding material particles conveyed upwards from the gas flow and to feed them directly back into the grinding process by gravity. So that the introduced from below into the packing of grinding media gas stream loosens this pack and discharges up the Mahlgutp personality at the top of the mill, the gas must have a considerable pressure.
  • this package must be relatively open-pored, ie the size of the grinding media is limited down.
  • the material to be ground must be relatively coarse. This in turn means that the spaces between the individual grinding bodies are insufficiently filled with regrind.
  • the energy consumption for the pressure blower is very high and is of the same order of magnitude as the energy consumption of the drive motor for the actual grinding process.
  • a tower grate mill known in which the ground material is introduced from above into the grinding container and discharged in the region of the bottom through a sieve.
  • a fluid for example in the form of air
  • a comparable tower friction mill is from the JP 2003 181 316 A known.
  • the sieve holes or sieve gaps in the bottom area can become clogged by worn or broken grinding media. This in turn leads to increased wear, which can eventually lead to damage to the lower ends of the screw webs.
  • Another disadvantage is that well-flowing ground material, such as dry quartz sand, flows very quickly through the MahlSystempackung and thus is not subjected to a controlled grinding process.
  • the invention has for its object to provide a method of the generic type and a tower grate mill of the generic type, in which a continuous dry grinding operation while maintaining the packing of grinding media in the grinding container is possible and in which the Use of relatively small grinding media and a high fineness of the ground material to be ground is achieved.
  • the packing of grinding media is dense during the entire grinding process, as it is not loosened from below, for example by gas.
  • the grinding bodies are conveyed upwards in the area covered by at least one screw land and accordingly flow downwards in the area not covered by the screw land, which is bounded externally by the grinding tank.
  • the millbase is thus at least once fully funded by the grinding media package from top to bottom and once from bottom to top and thereby subjected to a grinding process.
  • the media package Due to the conveying effect of the worm web in the region of the drive shaft, the media package is raised in the interior of the grinding container and forms an approximately frusto-conical, sloping outward surface, over which the grinding media roll to the outside. In this case, they press out the grinding stock on the surface or in the surface through the grinding stock outlet from the grinding container, whereby this is still supported to a considerable extent by the gas flow.
  • the tower grate mill shown in the drawing has a closed top, cylindrical grinding container 1, for whose inner diameter D applies: 0.4 m ⁇ D ⁇ 4.0 m.
  • a screw conveyor 2 is arranged as a grinding-body circulation device, which is arranged coaxially to the vertical center axis 3 of the grinding container 1.
  • the Screw conveyor 2 has a coaxial with the central axis 3 arranged drive shaft 4 with a diameter di on which two mutually parallel screw webs 5 with a slope s and an outer diameter da and an upper end 6 are attached.
  • the shaft 4 is rotationally driven by means of an electric motor 7 in a rotational direction 8.
  • the screw conveyor 4 extends down to the immediate vicinity of the bottom 9 of the grinding container 1.
  • the screw-webs 5 extend from this neighborhood to the bottom 9 over a height hs.
  • the tower grinder mill is very slim. For the ratio of the screw height hs to the diameter D of the grinding container 1, 1.5 ⁇ hs / D ⁇ 3.
  • a closed during operation MahlSystem outlet 10 is provided in the vicinity of the bottom 9 of the grinding container 1 in the latter.
  • a grinding stock outlet 11 is formed on the grinding container 1, to which a grinding stock removal line 12 connects.
  • a grinding media retention device in the form of a gap-sieve 14 is arranged, which in the 4 and 5 is shown. It has between approximately parallel to the central axis 3 extending webs 15 column 16, which - as out Fig. 4 can be seen - extend radially to the axis 3 to the outside and continue to expand from bottom to top, as from Fig. 5 seen. At least in the lower region, its width w is smaller than the diameter d 17 of the smallest grinding media 17 used.
  • the outlet opening 13 has a height h13.
  • the worm webs 5 extend from 0.1 h 13 to 0.5 h 13 over the lower edge 18 of the outlet opening 13, ie its upper end 6 is located at this height above the Bottom edge 18.
  • the cross-sectional area swept by the screw lands 5 is (da 2 - di 2 ) x ⁇ / 4.
  • the free annular cross-sectional area between the worm webs 5 and the grinding container is (D 2 - da 2 ) x ⁇ / 4.
  • the free cross-sectional area between the worm webs 5 and the grinding container 1 should be greater than or at most equal to the swept by the worm webs 5 annular cross-section. The following applies: (D 2 - da 2 ) ⁇ (da 2 - di 2 ) .
  • Fig. 1 opens a Mahlgut inlet 19 diametrically opposite the Mahlgut-outlet 11 in the grinding container 1 a. It is arranged above the upper end 6 of the worm webs 5, specifically starting above the upper edge 20 of the outlet opening 13.
  • the grinding stock inlet 19 is preceded by a grinding material feed line 21 into which the grinding material 22 is gas-tight Dosing device 23, for example, a rotary valve, is supplied.
  • a gas inlet 24 open to the atmosphere in this case an air inlet, is provided.
  • the regrind discharge line 12 is connected to a suction fan 25, with the interposition of a wind sifter 26, for example, a conventional cyclone separator, and a downstream of this dust filter separator 27.
  • a wind sifter 26 for example, a conventional cyclone separator
  • a Filter 28 is provided in the separator 27 . It is connected to the bottom of a gas-tight lock 29, such as a rotary valve. From the wind sifter 26 is coarse material to be ground via a return line 30 of the metering device 23 and thus fed to the grinding stock inlet 19 again.
  • the millbase discharged from the separator 27 has the desired fineness.
  • a pressure transducer 31 is arranged in the grinding container 1.
  • a further pressure transducer 32 is arranged in the regrind discharge line 12 relatively close behind the grinding stock outlet 11. Their pressure readings are applied to a differential pressure gauge 33 for determining the pressure difference between the two measured values.
  • a gas volume meter 34 is disposed between the separator 27 and the blower 25.
  • an additional gas line 35 which can be opened or closed via a controllable valve 36, opens into the grinding stock removal line 12 in the vicinity of the grinding stock outlet 11. About this additional gas can be introduced into the conduit 12 when the gas volume flow coming from the grinding container 1 is not sufficient to remove the ground material.
  • a gas flow meter 37 is inserted in this line 35.
  • the grinding container 1 Before commissioning the grinding container 1 is filled with grinding media 17, up to a height which is 80% to 95% of the height of the grinding container 1 to the upper end 6 of the screw webs 5 to just above the lower edge 18 of the outlet opening thirteenth is. Subsequently, the motor 7 is set in operation, so that the shaft 4 is set with the worm webs 5 in the direction of rotation 8 in operation. Corresponding to the pitch of the worm webs 5, the grinding bodies 17, which are located in the annular cross-sectional area of the grinding container 1 swept by the worm webs 5, are conveyed upwards.
  • the worm webs 5 are in proportion to the pitch s to the outer diameter da screw flights 5 0.5 da ⁇ s ⁇ 1.5 da and preferably 0.8 da ⁇ s ⁇ 1.2 da. Furthermore, the shaft 4 is driven with the worm webs 5 at such a speed that the worm webs 5 an outer peripheral speed of 2.0 to 4.0 m / sec and preferably between 2.2 and 3.0 m / sec.
  • the diameter d17 of the grinding bodies 17 the following applies: 10 mm ⁇ d17 ⁇ 30 mm and preferably 15 mm ⁇ d17 ⁇ 25 mm.
  • the supplied millbase 22 generally has a particle size which is smaller than 0.25 d17 of the diameter d17 of the grinding bodies 17 and preferably less than 0.2 d17. Since the grinding media 17 are conveyed upwards in the region of the screw flights 5, they sink downwards in the outer region not swept by the screw flights 5, as indicated by the circulation flow arrows 38 in FIG Fig. 1 is indicated. The millbase fed in the area of the container wall flows downwards with the grinding bodies 17 and is crushed between them. Connecting ⁇ end it is promoted again with further comminution with the grinding media 17 in the area of the screw webs 5 upwards.
  • the grinding media 17 are only slightly, up to 0.3 h 13, above the lower edge 18 of the outlet opening 13 and the screen 14.
  • regrind 22 which swells radially outward from the packing of grinding media 17, directly in front of the sieve 14.
  • air is sucked in from outside through the gas inlet 24 by the blower 25 and flows around the shaft 4 in accordance with the deflection arrow 40 and over the surface 39 of the grinding-body packing.
  • the gas inlet 24 is predominantly orthogonal, ie substantially directed to the axis 3, then only a simple deflection by 180 ° of the air around the shaft 4. If, however, the gas inlet 24 is arranged predominantly tangentially, then forms a rotational flow out.
  • the conveyed according to the deflection arrow 40 through the grinding container 1 air takes very fine ground material 22, which is fed through the Mahlgut inlet 19, directly with and carries it directly.
  • the gas stream enters the regrind discharge line 12 through the sieve 14.
  • the described gas flow in this case pushes the grinding material 22 located in the grinding container 1 in front of the sieve 14 into the line 12. As far as grinding bodies 17 reach the sieve 14, they are retained by this.
  • the entire material to be ground 22 is discharged after a described circulation.
  • the coarse grinding stock 22 which has not yet been sufficiently comminuted is separated off and returned to the grinding process by the return line 30 and via the metering device 23.
  • the conveying air enters together with the finely ground material to be ground 22 in the dust filter 27, where the finely ground material is deposited on the filter 28 and discharged through the lock 29.
  • the freed from the material to be ground 22 air is discharged through the blower 25.
  • the air additionally can be added via the additional gas line 35 of the conveying air.
  • the design of the actual tower friction mill after Fig. 2 is different from the after Fig. 1 by the arrangement of the gas inlet 24 '. This is located opposite the regrind outlet 11 above the millbase inlet 19.
  • the air flow flows around here corresponding to the flow arrow 41, the shaft 4 and then - as in the embodiment according to Fig. 1 over the surface 39 of the grinding material-MahlSystem-packing and presses the ground material 22 through the sieve 14 in the Mahlgut-discharge line 12.
  • the gas inlet 24 'in the direction of the shaft 4 is moved into the grinding container 1, so that the entering through the Mahlgut inlet 19 Mahlgut 22 can flow directly to the inner wall of the grinding container 1 down into the grinding media package.
  • Fig. 3 differs from the two previously illustrated in that the gas flow is not sucked by means of a suction fan. Rather, a pressure blower 42 is provided, which pushes gas with an arbitrary predeterminable pressure through a gas inlet 24 "from above into the grinding container 1. The gas flows according to the flow arrow 43 from above through the grinding container 1 and then over the Surface 39 to the grinding stock outlet 11 and presses in the manner already described, the material to be ground 22 through the sieve 14th
  • any pressure can be adjusted. So that according to the flow arrow 43 in the grinding container 1 after Fig. 3 inflowing gas does not pass through the grinding stock inlet 19 regrind 22nd entrains or swirled above the media package, the Mahlgut inlet 19 is covered by a guide plate 44 so that the Mahlgut-entry is not affected by the gas flow.
  • a guide plate 44 to cover the grinding stock inlet 19 in the embodiments of the Fig. 1 and 2 be used if necessary.
  • the grinding media outlet 10 ' is provided in the bottom 9 of the grinding container 1, whereby the removal of the grinding media 17 from the grinding container 1 can be facilitated.
  • a difference-pressure measurement is made via the measuring device 33 and the corresponding measured value is passed to a central control unit 45. If the measured differential pressure exceeds a predetermined setpoint, this may be an indication that the screen 14 is partially or completely clogged.
  • the fan unit 25 or the blower 42 can be controlled by the control unit 45 in order to increase and / or the main gas volume flow, which is supplied via the gas inlet 24, 24 'or 24 " The aim is to suck in more gas through the sieve 14 in such a case.
  • a main gas flow rate through the meter 34 which are promoted by the fan 25 and 42, respectively should.
  • the secondary gas volume flow to be supplied via the additional gas line 35 is adjusted so that a predetermined desired gas volume flow is conveyed through the grinding container 1. This funded by the grinding container 1 target gas flow rate results from the difference of the main gas volume flow and the secondary gas flow rate. If the gas volume flows are constantly measured via the measuring devices 34 and 37, it follows from an increase in the volume flow detected by the measuring device 37 that the screen 14 is partially or completely blocked. In such a case, the total gas volume flow to be delivered by the fan 25 or 42 is increased. At the same time, the valve 36 is partially or completely closed to achieve in this way a higher gas flow rate through the grinding container 1, and thus to blow the screen 14. Cumulatively, the already described differential pressure measurement can also be used.

Claims (15)

  1. Procédé pour le fonctionnement du broyage à sec en continu d'une tour de broyage par friction qui
    présente
    - un conteneur de broyage (1) vertical, fermé,
    - un transporteur à vis (2), disposé au centre du conteneur de broyage (1), comprenant
    -- un arbre d'entraînement (4) avec un axe central (3) et
    -- au moins un filet de vis (5), rapporté sur l'arbre d'entraînement (4), s'étendant au-delà d'une hauteur (hs) jusqu'à une extrémité supérieure (6), ne recouvrant la section transversale du conteneur de broyage (1) que partiellement,
    - un ensemble constitué de corps de broyage (17) comportant une surface supérieure (39),
    - une entrée de produit de broyage (19) débouchant dans le conteneur de broyage (1) au dessus de l'ensemble constitué par les corps de broyage (17),
    - une entrée de gaz (24, 24', 24") débouchant dans le conteneur de broyage (1) pour l'introduction de gaz,
    - une sortie de produit de broyage (11) débouchant du conteneur de broyage (1), présentant un bord inférieur (18) et une hauteur (h13), pour l'évacuation du produit de broyage (22) et du gaz, et
    - un moteur (7) pour l'entraînement du transporteur à vis (2) dans une direction de rotation (8) dans laquelle au moins un filet de vis (5) transporte le corps de broyage (17) vers le haut, caractérisé en ce
    - que la surface (39) de l'ensemble constitué par les corps de broyage (17), lors du fonctionnement en rotation du transporteur à vis (2), est configurée à peu près dans une forme émoussée de quille, tombant radialement vers l'extérieur et terminant radialement à l'extérieur de la zone du bord inférieur (18) de la sortie de produit de broyage (11),
    - que le gaz est introduit au dessus de l'ensemble constitué par les corps de broyage (17) dans le conteneur de broyage (1), et
    - que le gaz et le produit de broyage (22) sont évacués du conteneur de broyage (1) dans la zone de la surface (39) de l'ensemble constitué des corps de broyage (17) par la sortie de produit de broyage (3).
  2. Procédé selon la revendication 1 caractérisé en ce
    que le produit de broyage (22) est introduit dans le conteneur de broyage (1) en face de la sortie de produit de broyage (11).
  3. Procédé selon les revendications 1 ou 2 caractérisé en ce
    que le gaz est emmené au dessus de l'ensemble constitué par les corps de broyage (17), moyennant une déviation vers la surface (39) de l'ensemble constitué par les corps de broyage (17).
  4. Procédé selon l'une des revendications 1 à 3 caractérisé en ce
    que le gaz est passé devant l'entrée de produit de broyage (19).
  5. Procédé selon les revendications 1 ou 2 caractérisé en ce
    que le gaz est introduit dans le conteneur de broyage (1) en face de la sortie de produit de broyage (11).
  6. Procédé selon l'une des revendications de 1 à 5 caractérisé en ce
    que le gaz est évacué du conteneur de broyage (1) par aspiration.
  7. Procédé selon l'une des revendications de 1 à 5 caractérisé en ce
    que le gaz est introduit dans le conteneur de broyage insufflé sous pression.
  8. Procédé selon l'une des revendications de 1 à 7 caractérisé en ce
    que le transporteur à vis (2) est entraîné de telle manière qu'au moins un filet de vis (5) présente au niveau de sa circonférence extérieure une vitesse circonférentielle de 2,0 à 4,0 m/sec, de préférence de 2,2 à 3,0 m/sec.
  9. Procédé selon la revendication 1 caractérisé en ce
    que l'ensemble constitué par les corps de broyage (17) est réglé jusqu'à une hauteur (h13) s'arrêtant au maximum à 0,3h13 au dessus du bord inférieur (18) de la sortie du produit de broyage (11).
  10. Tour de broyage par friction qui présente
    - un conteneur de broyage (1) vertical, fermé,
    - un transporteur à vis (2), disposé au centre du conteneur de broyage (1), comprenant
    -- un arbre d'entraînement (4) avec un axe central (3) et
    -- au moins un filet de vis (5), rapporté sur l'arbre d'entraînement (4), s'étendant au-delà d'une hauteur (hs) jusqu'à une extrémité supérieure (6), ne recouvrant la section transversale du conteneur de broyage (1) que partiellement,
    - un ensemble constitué de corps de broyage (17) comportant une surface supérieure (39),
    - une entrée de produit de broyage (19) débouchant dans le conteneur de broyage (1) au dessus de l'ensemble constitué des corps de broyage (17),
    - une entrée de gaz(24, 24', 24") débouchant dans le conteneur de broyage (1) pour l'introduction de gaz,
    - une sortie de produit de broyage (11) débouchant du conteneur de broyage (1), présentant un bord inférieur (18) et une hauteur (h13), pour l'évacuation du produit de broyage (22) et du gaz, et
    - un moteur (7) pour l'entraînement du transporteur à vis (2) dans une direction de rotation (8) dans laquelle au moins un filet de vis (5) transporte le corps de broyage (17) vers le haut, caractérisée en ce
    - que la sortie de produit de broyage (11) présente une ouverture de sortie (13) comportant un tamis (14),
    - que l'extrémité supérieure (6) d'au moins un filet de vis (5) est disposée à la hauteur du tamis (14), et
    - que l'entrée de gaz (24, 24', 24") est disposée au dessus de l'extrémité supérieure (6) d'au moins un filet de vis (5).
  11. Tour de broyage par friction selon la revendication 10 caractérisée en ce
    que l'entrée de gaz (24) est disposée au dessus de la sortie de produit de broyage (11).
  12. Tour de broyage par friction selon la revendication 10 caractérisée en ce
    que l'entrée de gaz (24') est disposée en face de la sortie de produit de broyage (11) et au dessus de l'entrée de produit de broyage (19).
  13. Tour de broyage par friction selon la revendication 10 caractérisée en ce
    que l'entrée de gaz (24") débouche par le haut dans le conteneur de broyage (1).
  14. Tour de broyage par friction selon l'une des revendications 10 à 13 caractérisée en ce
    qu'un déflecteur de gaz (44) est prévu avant l'entrée de produit de broyage (19).
  15. Tour de broyage par friction selon l'une des revendications 10 à 14 caractérisée en ce
    que le tamis (14) est conçu comme un tamis à fente.
EP08700982.5A 2007-02-02 2008-01-04 Procédé pour fonctionnement de broyage à sec en continu d'une tour de broyage par friction et tour de broyage par friction Not-in-force EP2125230B8 (fr)

Priority Applications (1)

Application Number Priority Date Filing Date Title
PL08700982T PL2125230T3 (pl) 2007-02-02 2008-01-04 Sposób mielenia na sucho w ruchu ciągłym w wieżowym młynie rozcierającym oraz wieżowy młyn rozcierający

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
DE102007005250A DE102007005250B3 (de) 2007-02-02 2007-02-02 Verfahren zum kontinuierlichen Trockenmahlbetrieb einer Turmreibmühle und Turmreibmühle
PCT/EP2008/000030 WO2008092542A1 (fr) 2007-02-02 2008-01-04 Procédé pour fonctionnement de broyage à sec en continu d'une tour de broyage par friction et tour de broyage par friction

Publications (3)

Publication Number Publication Date
EP2125230A1 EP2125230A1 (fr) 2009-12-02
EP2125230B1 true EP2125230B1 (fr) 2013-06-05
EP2125230B8 EP2125230B8 (fr) 2013-07-17

Family

ID=38825521

Family Applications (1)

Application Number Title Priority Date Filing Date
EP08700982.5A Not-in-force EP2125230B8 (fr) 2007-02-02 2008-01-04 Procédé pour fonctionnement de broyage à sec en continu d'une tour de broyage par friction et tour de broyage par friction

Country Status (17)

Country Link
US (2) US7971808B2 (fr)
EP (1) EP2125230B8 (fr)
JP (1) JP5358457B2 (fr)
KR (1) KR101381488B1 (fr)
CN (1) CN101600504B (fr)
AU (1) AU2008210059B2 (fr)
BR (1) BRPI0806627A2 (fr)
CA (1) CA2677268C (fr)
DE (1) DE102007005250B3 (fr)
DK (1) DK2125230T3 (fr)
ES (1) ES2424021T3 (fr)
MX (1) MX2009007307A (fr)
PL (1) PL2125230T3 (fr)
RU (1) RU2453372C2 (fr)
UA (1) UA97510C2 (fr)
WO (1) WO2008092542A1 (fr)
ZA (1) ZA200905382B (fr)

Families Citing this family (17)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE102007005250B3 (de) * 2007-02-02 2008-01-17 Maschinenfabrik Gustav Eirich Gmbh & Co. Kg Verfahren zum kontinuierlichen Trockenmahlbetrieb einer Turmreibmühle und Turmreibmühle
CN101954305A (zh) * 2010-09-25 2011-01-26 昆山密友粉碎设备有限公司 干法搅拌研磨机
WO2013167851A1 (fr) * 2012-05-10 2013-11-14 Belmonte Investments Limited Broyeur par frottement et son procédé d'utilisation
DE102012013279A1 (de) * 2012-07-05 2014-01-09 Roland Nied Verfahren zum Betrieb einer Rührwerkskugelmühle sowie Rührwerkskugelmühle dafür
CN102728440B (zh) * 2012-07-11 2014-04-16 北京萃宝重工科技有限公司 高效立式球磨机
US9764329B2 (en) * 2013-01-15 2017-09-19 Aaron Engineered Process Equipment, Inc. Rotary mill
EP2837424A1 (fr) * 2013-08-13 2015-02-18 TARTECH eco industries AG Briseur de scories
US9943853B2 (en) * 2014-01-16 2018-04-17 Michael Marshall Pulverizing apparatus and method of pulverizing rocks
US10058872B2 (en) 2014-07-03 2018-08-28 STT Enviro Corp. Vertical ball mill with internal materials flow conduit
DE102015200924A1 (de) * 2015-01-21 2016-07-21 Robert Bosch Gmbh Koaxialmühle und Zufuhreinheit für eine Mühle
US10500591B2 (en) * 2015-09-02 2019-12-10 Air Products And Chemicals, Inc. System and method for the preparation of a feedstock
US10926269B2 (en) * 2017-12-01 2021-02-23 Metso Minerals Industries, Inc. Vertical grinding mill, screw shaft, and method of designing and/or manufacturing a screw shaft
CN108816395A (zh) * 2018-08-09 2018-11-16 洛阳矿山机械工程设计研究院有限责任公司 一种立式搅拌磨的变螺距螺旋搅拌器
CN111135912A (zh) * 2020-01-15 2020-05-12 厦门艾思欧标准砂有限公司 一种干法研磨与整形的节能型立式研磨机
CN111420780B (zh) * 2020-01-15 2022-03-01 厦门艾思欧标准砂有限公司 一种立式研磨机研磨与整形的方法
CN113019645B (zh) * 2021-03-22 2022-09-09 江苏巨胜智能传动科技有限公司 一种乌龟养殖用产蛋沙处理装置
CN115446320B (zh) * 2022-09-06 2023-06-27 江苏威拉里新材料科技有限公司 一种金属颗粒循环研磨装置及其使用方法

Family Cites Families (27)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE1242078B (de) * 1962-06-13 1967-06-08 Spangenberg Maschf G Ruehrwerksmuehle zum fortlaufenden Mahlen und Dispergieren von Stoffen in Fluessigkeiten
US3350280A (en) * 1963-10-31 1967-10-31 Standard Oil Co Retort for oil-bearing shales
DE1507653C3 (de) 1966-06-10 1975-05-07 Gustav Spangenberg Maschinenfabrik Gmbh, 6800 Mannheim Vorrichtung zum fortlaufenden Mahlen und Dispergieren von Stoffen in Flüssigkeiten
JPS60155957U (ja) * 1984-03-28 1985-10-17 日本タワ−ミル株式会社 塔型摩砕粉砕機の生産物排出装置
JPS60161443U (ja) * 1984-04-04 1985-10-26 日本タワ−ミル株式会社 塔型摩砕粉砕機の生産物選別排出装置
DD268892A1 (de) * 1986-11-28 1989-06-14 Akad Wissenschaften Ddr Vorrichtung und verfahren zur fein- und feinstmahlung
JPH043630Y2 (fr) * 1987-01-23 1992-02-04
JPS63200849A (ja) * 1987-02-16 1988-08-19 株式会社　井上製作所 連続式原料細分化方法及び装置
KR900002381Y1 (ko) * 1987-04-08 1990-03-26 구보다뎃고오 가부시기가이샤 마쇄분쇄 장치
JPH01120949U (fr) * 1988-02-09 1989-08-16
US5167375A (en) * 1988-04-04 1992-12-01 Datta Rabinder S Apparatus for mineral matter separation
JP2976481B2 (ja) * 1989-05-10 1999-11-10 松下電器産業株式会社 フィルム状グラファイトの製造方法
JPH0389953A (ja) * 1989-08-31 1991-04-15 Mitsui Miike Kakoki Kk 乾式粉砕方法
AU626758B2 (en) * 1990-07-23 1992-08-06 Kubota Corporation Pulverizer
JPH0441733U (fr) * 1990-08-09 1992-04-09
DE4202101A1 (de) * 1992-01-27 1993-07-29 Zementanlagen Und Maschinenbau Verfahren und vorrichtung zum behandeln von trockenem bis feuchtem material
AU656843B2 (en) * 1992-03-30 1995-02-16 Kubota Corporation Vertical pulverizer
JPH0585447U (ja) * 1992-04-22 1993-11-19 三井三池化工機株式会社 粉砕機
JP2566884Y2 (ja) * 1992-05-27 1998-03-30 三井鉱山株式会社 粉砕機
JPH07256133A (ja) * 1994-03-25 1995-10-09 Kubota Corp 摩砕粉砕
JP3231538B2 (ja) 1994-03-25 2001-11-26 株式会社クボタ 竪型媒体撹拌粉砕機の処理筒内面保護構造
JP3239671B2 (ja) * 1995-03-08 2001-12-17 松下電器産業株式会社 フィルム状ヒーター、保温座席、蒸着ボートおよび加熱炉
JP2002333274A (ja) * 2001-05-10 2002-11-22 Taikisha Ltd 熱風式乾燥装置、及び、それを用いた生ごみ処理方法
JP2003181316A (ja) * 2001-12-17 2003-07-02 Nippon Airitsuhi Kk 媒体撹拌粉砕装置およびこの装置を有する粉砕処理システム
JP2005246204A (ja) * 2004-03-03 2005-09-15 Kubota Construction Co Ltd 粉砕用ボールを用いた粉砕方法
JP2006154802A (ja) * 2004-11-08 2006-06-15 Canon Inc 像加熱装置及びこの装置に用いられるヒータ
DE102007005250B3 (de) * 2007-02-02 2008-01-17 Maschinenfabrik Gustav Eirich Gmbh & Co. Kg Verfahren zum kontinuierlichen Trockenmahlbetrieb einer Turmreibmühle und Turmreibmühle

Also Published As

Publication number Publication date
ES2424021T3 (es) 2013-09-26
RU2453372C2 (ru) 2012-06-20
US8141801B2 (en) 2012-03-27
US7971808B2 (en) 2011-07-05
DK2125230T3 (da) 2013-09-08
MX2009007307A (es) 2009-08-07
US20100102151A1 (en) 2010-04-29
BRPI0806627A2 (pt) 2011-09-13
CA2677268C (fr) 2014-07-08
DE102007005250B3 (de) 2008-01-17
EP2125230A1 (fr) 2009-12-02
CN101600504A (zh) 2009-12-09
PL2125230T3 (pl) 2013-11-29
ZA200905382B (en) 2010-10-27
CN101600504B (zh) 2011-06-15
CA2677268A1 (fr) 2008-08-07
JP5358457B2 (ja) 2013-12-04
KR20090115160A (ko) 2009-11-04
UA97510C2 (ru) 2012-02-27
AU2008210059B2 (en) 2011-08-11
EP2125230B8 (fr) 2013-07-17
US20110240774A1 (en) 2011-10-06
JP2010517739A (ja) 2010-05-27
WO2008092542A1 (fr) 2008-08-07
KR101381488B1 (ko) 2014-04-04
AU2008210059A1 (en) 2008-08-07
RU2009128952A (ru) 2011-03-10

Similar Documents

Publication Publication Date Title
EP2125230B1 (fr) Procédé pour fonctionnement de broyage à sec en continu d'une tour de broyage par friction et tour de broyage par friction
EP2764808B1 (fr) Broyeur
DE4447321C2 (de) Rührwerksmühle für die nasse Feinzerkleinerung, mit Separator zur Zurückhaltung von Mahlperlen
DE4432200C1 (de) Rührwerksmühle
DE3311433A1 (de) Klassieren von mahlgut von vertikalen rollenmuehlen
EP2155353B1 (fr) Séparateur à vis à pression
EP1468739A1 (fr) Broyeur agitateur à billes
EP0460490B1 (fr) Séparateur pneumatique
DD288987A5 (de) Ruehrwerkskugelmuehle
DE8425837U1 (de) Wälzmühle
DE1286386B (de) Schlaeger- oder Schleuderprallmuehle mit Sichter
WO2009024159A1 (fr) Broyeur agitateur
EP0700721B1 (fr) Broyeur agitateur
DE3811910C2 (de) Mühle und Verfahren zum gleichzeitigen Mahlen und Trocknen eines feuchten Produkts
EP1080786A1 (fr) Procédé, dispositif et système pour broyeur à jet à lit fluidisé
DE19948727A1 (de) Kreislaufmahleinrichtung mit Hochdruck-Walzenmühle und Sichter
CH660073A5 (de) Vakuum-trocken-vorrichtung.
DE10139413A1 (de) Vorrichtung zum Mischen und Dispergieren von pulverförmigen feinst- bis grobkörnigen Substanzen mit mindestens einer Flüssigkeit
EP0700724B2 (fr) Procédé et appareil pour le broyage continu autogène d'une matière à traiter fluide
EP3541523A1 (fr) Broyeur
DE4402609C1 (de) Rührwerkskugelmühle
DE3222890A1 (de) Pulvermuehlen-vorrichtung
EP1350569B1 (fr) Séparateur de déchets
DE1245257B (de) Vorrichtung zum Zerkleinern von insbesondere festen, koernerartigen Stoffen
DE666249C (de) Mit losen Mahlkoerpern arbeitende Mahlvorrichtung

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: 20090703

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 HR HU IE IS IT LI LT LU LV MC MT NL NO PL PT RO SE SI SK TR

DAX Request for extension of the european patent (deleted)
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): AT BE BG CH CY CZ DE DK EE ES FI FR GB GR HR HU IE IS IT LI LT LU LV MC MT NL NO PL PT RO SE SI SK TR

REG Reference to a national code

Ref country code: GB

Ref legal event code: FG4D

Free format text: NOT ENGLISH

REG Reference to a national code

Ref country code: CH

Ref legal event code: EP

REG Reference to a national code

Ref country code: AT

Ref legal event code: REF

Ref document number: 615318

Country of ref document: AT

Kind code of ref document: T

Effective date: 20130615

REG Reference to a national code

Ref country code: SE

Ref legal event code: TRGR

RAP2 Party data changed (patent owner data changed or rights of a patent transferred)

Owner name: MASCHINENFABRIK GUSTAV EIRICH GMBH & CO. KG

REG Reference to a national code

Ref country code: IE

Ref legal event code: FG4D

Free format text: LANGUAGE OF EP DOCUMENT: GERMAN

REG Reference to a national code

Ref country code: DE

Ref legal event code: R096

Ref document number: 502008010069

Country of ref document: DE

Effective date: 20130801

REG Reference to a national code

Ref country code: RO

Ref legal event code: EPE

REG Reference to a national code

Ref country code: DK

Ref legal event code: T3

REG Reference to a national code

Ref country code: ES

Ref legal event code: FG2A

Ref document number: 2424021

Country of ref document: ES

Kind code of ref document: T3

Effective date: 20130926

REG Reference to a national code

Ref country code: NO

Ref legal event code: T2

Effective date: 20130605

REG Reference to a national code

Ref country code: GR

Ref legal event code: EP

Ref document number: 20130401727

Country of ref document: GR

Effective date: 20130920

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: LT

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20130605

Ref country code: SI

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20130605

Ref country code: FI

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20130605

REG Reference to a national code

Ref country code: NL

Ref legal event code: VDEP

Effective date: 20130605

REG Reference to a national code

Ref country code: LT

Ref legal event code: MG4D

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: BG

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20130905

Ref country code: HR

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20130605

REG Reference to a national code

Ref country code: PL

Ref legal event code: T3

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: LV

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20130605

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: PT

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20131007

Ref country code: EE

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20130605

Ref country code: SK

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20130605

Ref country code: IS

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20131005

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: NL

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20130605

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: 20140306

REG Reference to a national code

Ref country code: DE

Ref legal event code: R097

Ref document number: 502008010069

Country of ref document: DE

Effective date: 20140306

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: MC

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20130605

Ref country code: LU

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20140104

REG Reference to a national code

Ref country code: IE

Ref legal event code: MM4A

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: IE

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20140104

REG Reference to a national code

Ref country code: FR

Ref legal event code: PLFP

Year of fee payment: 9

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: MT

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20130605

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: CY

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20130605

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: HU

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT; INVALID AB INITIO

Effective date: 20080104

REG Reference to a national code

Ref country code: FR

Ref legal event code: PLFP

Year of fee payment: 10

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: CH

Payment date: 20161207

Year of fee payment: 10

Ref country code: CZ

Payment date: 20161227

Year of fee payment: 10

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: PL

Payment date: 20161208

Year of fee payment: 10

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: RO

Payment date: 20170103

Year of fee payment: 10

Ref country code: NO

Payment date: 20170123

Year of fee payment: 10

Ref country code: SE

Payment date: 20170125

Year of fee payment: 10

Ref country code: FR

Payment date: 20170124

Year of fee payment: 10

Ref country code: GR

Payment date: 20170124

Year of fee payment: 10

Ref country code: DE

Payment date: 20170327

Year of fee payment: 10

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: BE

Payment date: 20170124

Year of fee payment: 10

Ref country code: AT

Payment date: 20161209

Year of fee payment: 10

Ref country code: DK

Payment date: 20170125

Year of fee payment: 10

Ref country code: GB

Payment date: 20170125

Year of fee payment: 10

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: IT

Payment date: 20170125

Year of fee payment: 10

Ref country code: ES

Payment date: 20170124

Year of fee payment: 10

Ref country code: TR

Payment date: 20170102

Year of fee payment: 10

REG Reference to a national code

Ref country code: DE

Ref legal event code: R119

Ref document number: 502008010069

Country of ref document: DE

REG Reference to a national code

Ref country code: DK

Ref legal event code: EBP

Effective date: 20180131

REG Reference to a national code

Ref country code: NO

Ref legal event code: MMEP

REG Reference to a national code

Ref country code: SE

Ref legal event code: EUG

REG Reference to a national code

Ref country code: CH

Ref legal event code: PL

REG Reference to a national code

Ref country code: AT

Ref legal event code: MM01

Ref document number: 615318

Country of ref document: AT

Kind code of ref document: T

Effective date: 20180104

GBPC Gb: european patent ceased through non-payment of renewal fee

Effective date: 20180104

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: SE

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20180105

Ref country code: DE

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20180801

Ref country code: RO

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20180104

Ref country code: NO

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20180131

Ref country code: FR

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20180131

REG Reference to a national code

Ref country code: FR

Ref legal event code: ST

Effective date: 20180928

REG Reference to a national code

Ref country code: BE

Ref legal event code: MM

Effective date: 20180131

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: AT

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20180104

Ref country code: LI

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20180131

Ref country code: GB

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20180104

Ref country code: CH

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20180131

Ref country code: BE

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20180131

Ref country code: CZ

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20180104

Ref country code: GR

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20180802

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: DK

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20180131

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: IT

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20180104

REG Reference to a national code

Ref country code: ES

Ref legal event code: FD2A

Effective date: 20190730

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: ES

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20180105

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: PL

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20180104

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: TR

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20180104