EP1724022B1 - Broyeur à agitateur - Google Patents

Broyeur à agitateur Download PDF

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Publication number
EP1724022B1
EP1724022B1 EP05010815A EP05010815A EP1724022B1 EP 1724022 B1 EP1724022 B1 EP 1724022B1 EP 05010815 A EP05010815 A EP 05010815A EP 05010815 A EP05010815 A EP 05010815A EP 1724022 B1 EP1724022 B1 EP 1724022B1
Authority
EP
European Patent Office
Prior art keywords
grinding
grinding chamber
mill according
agitator mill
chamber
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
EP05010815A
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German (de)
English (en)
Other versions
EP1724022A1 (fr
Inventor
Norbert Dr.-Ing. Stehr
Philipp Schmitt
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.)
Buehler AG
Original Assignee
Buehler AG
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
Priority to AT05010815T priority Critical patent/ATE361146T1/de
Application filed by Buehler AG filed Critical Buehler AG
Priority to ES05010815T priority patent/ES2285603T3/es
Priority to DE502005000670T priority patent/DE502005000670D1/de
Priority to EP05010815A priority patent/EP1724022B1/fr
Priority to US11/171,319 priority patent/US7216822B2/en
Priority to JP2006138920A priority patent/JP5010853B2/ja
Priority to KR1020060044818A priority patent/KR101245478B1/ko
Priority to CNB2006100826375A priority patent/CN100544892C/zh
Publication of EP1724022A1 publication Critical patent/EP1724022A1/fr
Application granted granted Critical
Publication of EP1724022B1 publication Critical patent/EP1724022B1/fr
Not-in-force legal-status Critical Current
Anticipated expiration legal-status Critical

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Classifications

    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B02—CRUSHING, PULVERISING, OR DISINTEGRATING; PREPARATORY TREATMENT OF GRAIN FOR MILLING
    • B02C—CRUSHING, PULVERISING, OR DISINTEGRATING IN GENERAL; MILLING GRAIN
    • 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
    • B02C17/166—Mills in which a fixed container houses stirring means tumbling the charge of the annular gap type
    • 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
    • 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
    • B02C17/08—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 containers performing a planetary movement

Definitions

  • the invention relates to a stirred mill according to the preamble of claim 1.
  • both the inner grinding chamber and the outer grinding chamber are smooth-walled without perforations and are free of stirring tools.
  • the gap width, ie the radial extent of the outer grinding chamber is significantly greater than that of the inner grinding chamber. This is intended to achieve that the grinding and dispersion of the flowable, slurried grind takes place predominantly by shear effects in such a way that the local stress intensity of the grind over the entire Mahlweg is substantially constant. Due to the smooth-walled configuration of the cylindrical boundary walls of the outer grinding chamber and the inner grinding chamber, a flow is generated in which the auxiliary grinding bodies are moved in layers relative to one another.
  • the shear gradient and thus the local stress intensity is constant in the outer grinding chamber on the one hand and in the inner grinding chamber on the other hand above the respective Mahlraumiere. Since the gap width of the inner grinding chamber is smaller than the gap width of the outer grinding chamber, the shear gradient in the outer grinding chamber and in the inner grinding chamber can be made the same size; it is then constant over virtually the entire grinding space. It has turned out to be problematical that, with a high grinding auxiliary body filling level, it is difficult to start up the agitator mill. Because of the problems with starting up the agitator mill, it is operated with a reduced grinding aid filling, which in turn leads to an unfavorably wide grinding stock particle size distribution.
  • the invention has for its object to design a stirred mill of the generic type so that the startup of the stirred mill easier and during operation a narrow grinding material particle size distribution is achieved.
  • the agitator mill can be operated with a high Mahltostage filling level, ie the Mahltostage filling need not be reduced. This in turn leads to a particularly intensive grinding while avoiding a grinding stock pass, since Mahlosterrorism be transported back in sufficient amount by the Mahlos stresses-return channels.
  • inventively desired effects are still particularly favorably influenced by the development according to claim 2, wherein the development according to claim 3 continues to be supportive.
  • the inner stator is provided in the region of the outflow channel according to claim 12 with a wear protection, which is particularly advantageous if the gap width of the outflow channel to the separating device, ie radially inwardly, not enlarged, so if the flow area is reduced with a corresponding acceleration of the Mahlgut Mahlosêt flow.
  • the agitator mill shown in Fig. 1 has in the usual way a stand 1, to which a cylindrical grinding container 2 can be attached.
  • an electric drive motor 3 is housed, which is provided with a V-belt pulley 4, of which via V-belt 5 with a drive shaft 6 rotatably connected V-belt pulley 7 is rotationally driven.
  • the grinding container 2 consists of a cylindrical inner wall 9 surrounding a grinding chamber 8, which is surrounded by a substantially cylindrical outer jacket 10.
  • the lower wall of the grinding chamber 8 is formed by an annular bottom plate 12, which is fastened to the grinding container 2 by means of screws 13.
  • the grinding container 2 has an upper annular flange 14, by means of which it is attached to the underside of a support housing 15 by means of screws 16 which is mounted on the stator 1 of the agitator mill.
  • the grinding chamber 8 is closed by means of a lid 17.
  • the support housing 15 has a central bearing and seal housing 18 which is arranged coaxially to the central longitudinal axis 19 of the grinding container 2. This bearing and seal housing 18 is penetrated by the likewise coaxial to the axis 19 extending drive shaft 6, to which a stirrer 20 is mounted. In the grinding chamber 8 adjacent region of the bearing and seal housing 18 opens a regrind supply line 21 a.
  • annular bottom plate 12 a projecting into the grinding chamber 8 approximately cup-shaped, cylindrical inner stator 22 is attached, consisting of a grinding chamber 8 bounding, coaxial to the axis 19, cylindrical outer shell 23 and a likewise coaxial to the axis 19, cylindrical inner shell 24 exists. They limit between a cooling space 25.
  • the cooling space 25 is connected to a cooling space 26 in the bottom plate 12, the cooling water via a cooling water supply port 27 is supplied, which is discharged via a cooling water discharge port 28.
  • the cooling space 11 of the grinding container 2 is supplied with cooling water via a cooling water supply pipe 29, which is discharged via a cooling water discharge pipe 30.
  • a Mahlgut Mahltosève-separating device 32 is arranged, which is connected to a regrind discharge line 33. Between the separator 32 and the drain line 33, a grinding stock hopper 34 is provided.
  • the drain line 33 is provided in the region of the bottom plate 12 with a mounting bracket 35, which is releasably connected by means of screws 36 with the bottom plate 12 and the fixedly connected to this inner stator 22.
  • the separating device 32 is sealed relative to the annular end portion 31 of the inner stator 22 by means of a seal 37 and can be pulled out after loosening the screws 36 together with the drain line 33 and the collecting hopper 34 from the inner stator 22 down.
  • the separating device 32 can thus be pulled out of the grinding chamber 8, without the Mahlospian located in this 38 must be removed from the grinding chamber 8, since the filling of the grinding chamber 8 with these Mahlos stressesn 38 with non-driven agitator 20 does not reach to the front part 31.
  • the agitator 20 is cup-shaped in its basic structure, ie it has a substantially annular cylindrical rotor 39.
  • the rotor 39 has a cylindrical inner wall 41, which has a cylindrical outer wall 40 and a coaxial with it and coaxial with the axis 19.
  • the outer wall 40 and the inner wall 41 are smooth-walled and as closed surfaces trained, so have no openings.
  • a cooling space 42 is formed between the outer wall 40 and the inner wall 41 of the rotor 39.
  • the agitator 20 is provided with a cover-like termination part 43, to whose bottom side facing the rotor 39, a closure plate 44 is attached.
  • the termination part 43 and the end plate 44 are attached to the drive shaft 6.
  • a Mahlospian-return module 45 is arranged between the rotor 39 and the end plate 44 of the agitator 20, a Mahlospian-return module 45 is arranged.
  • the rotor 39, the return module 45 and the end plate 44 are detachably connected together by tie rods 46.
  • an outer grinding chamber 8a is formed.
  • an inner grinding chamber 8b is limited.
  • this inner grinding chamber 8b protrude on the outer surface 23 of the inner stator 22 mounted, designed as a pin-shaped tools 49 surveys in which - as is apparent in particular from Fig. 4 - are arranged helically over the circumference and the length of the outer shell 23.
  • adjacent tools 49 in the circumferential direction of the inner stator 22 overlap one another in the direction of the central longitudinal axis 19 arranged so that in one revolution of the rotor 39 whose inner wall 41 is completely swept by the tools 49.
  • the grinding chamber 8 is thus divided into a cylindrical outer grinding chamber 8a on the one hand and a cylindrical annular grinding chamber 8b on the other hand, connected by a constantly widening from outside to inside deflection space 50 in the vicinity of the bottom plate 12 are.
  • the cylindrical separator 32 consists of a stack of annular disks 51, between each of which a separating gap 52 is left free, the width of which is generally smaller than the diameter of the smallest grinding auxiliary body 38 used; However, the width can also be greater, since the separation of the Mahlos stresses 38 takes place before reaching the separator 32.
  • the stack of annular discs 51 is the end side, ie at the end plate 44 facing side, completed by a closure plate 53.
  • the separator 32 is disposed within the return module 45.
  • the return channels 54 extend in the direction of the axis 19 almost over the full height of the return module 45, wherein its axial height e is greater than the axial height f of the separator 32.
  • Die Return channels 54 extend in this embodiment except via the separator 32 in the direction of the axis 19 still obliquely upward from the upper end of the inner grinding chamber 8b and inside to the separator 32 leading, so tapering in the direction of the end plate 44 towards frustoconical Outflow channel 59.
  • the return channels 54 are also open to the outflow channel 59, as Fig. 2 reveals.
  • the outflow channel 59 is therefore not spatially limited upwards. Rather, it is open in the direction of the central longitudinal axis 19 towards the internal grinding chamber 8b and thus permeable to the exit of the grinding auxiliary bodies 38, while the millbase flows through the outflow channel 59 in the direction of the separating device 32.
  • the material to be ground flows through the grinding chamber 8 corresponding to the flow direction arrows 60 coming from the grinding material supply line 21 through a Mahlgut feed chamber 61 between the end portion 43 of the agitator 20 on the one hand and the lid 17 and the adjacent region of the inner wall 9 on the other hand, the grinding material feed Area 57, the outer grinding chamber 8a down, by the steadily widening deflection space 50 radially inwardly and from there through the inner grinding chamber 8b after on the way up to the outflow channel 59 and from there to the separator 32.
  • the material to be ground is milled in rotationally driven agitator 20 in cooperation with the auxiliary grinding bodies 38.
  • the ground material leaves the interior grinding chamber 8 b through the separating device 32, from where it flows through the grinding stock discharge line 33.
  • FIGS. 6 and 7 differs from that of FIGS. 2 to 5 essentially in that between the end plate 44 and the rotor 39 except a Mahltospian feedback module 45 'still a jam device 62 is provided as part of the agitator 20'.
  • a jam device 62 is provided as part of the agitator 20'.
  • the inner grinding chamber 8b does not open at its upper end directly into the return channels 54 ', but instead feeds the grinding material.
  • Mahltosêt mixture is forced by the jam device 62 obliquely upwards and inwards in the direction of the separator 32 '.
  • the gap width j of the outflow channel 59 ' is constant.
  • the separating device 32 'does not extend over the full area above the end portion 31. Rather, a closed ring portion as wear protection 63 is provided between the end portion 31 and the separator 32', which is formed integrally with the separator 32 '. Before him or on him the outflow channel ends 59 ', so that from the outflow channel 59' exiting and deflected in an axis-parallel motion Mahltosève 38, the separator 32 'do not hit.
  • the embodiment according to FIG. 8 differs from that according to FIGS. 6 and 7 only in that the grinding aid return channels 54 "have a minimum required height e" for trouble-free operation at low grinding stock throughputs. Otherwise, the Mahlosterrorism feedback module 45 "includes here to the jam means 62, wherein in this embodiment, as in the two aforementioned embodiments, the return channels 54" are bounded on their upper side by the end plate 44. The axial height k is the same in the return modules 45 'and 45 ".
  • FIG. 9 corresponds to that of FIG. 6 with the difference that no wear protection 63 is provided and that on the other hand the outflow channels 59 '' extend towards the grinding aid separator 32, ie the gap width j '' of the outflow channel 59 '' increases inwards to such an extent that the total cross-sectional area of this channel 59 '' In any case, it does not become smaller in the direction of the separating device 32 so that there is no acceleration of the grinding stock auxiliary body flow in the outflow channel 59 '' to the separating device 32. For this reason, the separating device 32 can extend to the front part 31, since the auxiliary grinding bodies 38 do not hit the separator 32.
  • FIG. 10 substantially corresponds to that of FIG. 9, wherein the Mahlosève feedback module 45 "" is not brought up to the separator 32.
  • the inlet openings 55 “" of the grinding auxiliary body return channels 54 “” thus have a clear radial distance from the separating device 32.
  • this annular space 64 a plurality of scrapers 65 are provided, which are attached to the end plate 44 and rotate with the agitator 20 "".
  • the exemplary embodiment according to FIGS. 11 to 13 has a grinding aid body return module 45 ""'which bears against an intermediate ring 66 toward the accumulation device 62.
  • the module 45 “"' is thus down to the grinding chamber 8, ie to an end face 67, open.
  • the axial height e ""' is constant from the respective inlet opening 55 ""' to the outlet opening 56 ""'and is significantly smaller than the height f' of the separating device 32 '.

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  • Engineering & Computer Science (AREA)
  • Food Science & Technology (AREA)
  • Crushing And Grinding (AREA)
  • Mixers With Rotating Receptacles And Mixers With Vibration Mechanisms (AREA)

Claims (18)

  1. Broyeur à agitateur pour broyer des aliments pouvant se fluidifier, avec un récipient à aliments (2) délimitant un compartiment à aliments (8) largement fermé, à l'aide d'une paroi interne (9) et avec un agitateur (20) rotatif en forme de pot, placé dedans, relativement à un axe central (19) commun, avec un rotor (39) cylindrique qui présente une paroi (40, 41) fermée et avec stator interne (22) placé dans le rotor (39) et fixé au récipient à aliments (2), où, entre la paroi interne (9) du récipient à aliments (2) et une paroi externe (40) du rotor (39), se trouve un compartiment à aliments externe (8a) cylindrique, en fente annulaire, avec un interstice radial g et où, entre une paroi interne (41) du rotor (39) et une enveloppe externe (23) du stator interne (22), se trouve un compartiment à aliments interne (8b) cylindrique, en fente annulaire, coaxial à l'intérieur du compartiment à aliments externe (8a) et relié à celui-ci par un compartiment de renvoi (50), avec un interstice radial h, où le compartiment à aliments externe (8a), le compartiment de renvoi (50) et le compartiment à aliments interne (8b) forment le compartiment à aliments (8), en partie rempli de corps auxiliaires d'aliments (38), où se trouvent une zone d'alimentation (57) disposée avant le compartiment à aliments externe (8a), dans le sens de circulation (60) de l'aliment, débouchant dans celui-ci, et un dispositif de séparation (32) placé après le compartiment à aliments interne (8b) dans le sens de circulation (60), pour le passage de l'aliment à peu près du même côté du récipient à aliments (2), où, dans l'agitateur (20), sont prévus des canaux de retour de corps auxiliaires d'aliments (54) pour la recirculation des corps auxiliaires (38) de la zone du dispositif de séparation (32) vers la zone d'alimentation (57), qui relient l'extrémité finale du compartiment à aliments interne (8b) à l'extrémité de début du compartiment à aliments interne (8b) et où la paroi interne (9) du récipient à aliments (2) et la paroi externe (40) et la paroi interne (41) du rotor (39) ne sont pas ajourées et la paroi interne (9) du récipient à aliments (2) et la paroi externe (40) du rotor (39) sont lisses et n'ont pas d'outils agitateurs,
    caractérisé en ce que
    pour l'interstice radial g du compartiment à aliments externe (8a) par rapport à l'interstice radial h du compartiment à aliments interne (8b) on a :
    g < h.
  2. Broyeur à agitateur selon la revendication 1,
    caractérisé en ce que pour l'aire de la section transversale Fa du compartiment à aliments externe (8a) par rapport à l'air de la section transversale Fb du compartiment à aliments interne (8b), on a :
    Fa ≤ Fb et de préférence
    1,2 Fa ≤ Fb ≤ 7 Fa
  3. Broyeur à agitateur selon la revendication 1 ou 2, caractérisé en ce que pour l'interstice g du compartiment à aliments externe (8a) par rapport au diamètre i des plus gros corps auxiliaires (38) se trouvant dans le compartiment à aliments (8), on a : g ≥ 3i, où pour le diamètre i des corps auxiliaires (38) on a :
    i ≤ 3,0 mm et de préférence
    i ≤ 1,5 mm et
    où, pour l'interstice g du compartiment à aliments externe (8a) on a de plus :
    g ≤ 9,0 mm et de préférence
    g ≤ 5,0 mm
  4. Broyeur à agitateur selon l'une des revendications 1 à 3, caractérisé en ce que l'enveloppe externe (23) du stator interne (22) est équipée d'élévations ressortant dans le compartiment à aliments interne (8b).
  5. Broyeur à agitateur selon la revendication 4, caractérisé en ce que les élévations sont des outils (49), plus particulièrement des outils (49) en forme de tenons.
  6. Broyeur à agitateur selon la revendication 4, caractérisé en ce que les élévations sont disposées en hélice sur le stator interne (22).
  7. Broyeur à agitateur selon l'une des revendications 1 à 6, caractérisé en ce que la paroi interne (41) du rotor (39) est elle aussi lisse, sans agitateurs.
  8. Broyeur à agitateur selon l'une des revendications 1 à 7, caractérisé en ce qu'un canal d'écoulement (59) tronconique, dirigé vers le dispositif de séparation (32) de corps auxiliaires d'aliments, est raccordé au compartiment à aliments interne (8b).
  9. Broyeur à agitateur selon la revendication 8, caractérisé en ce que le canal d'écoulement (59) est délimité par un front (31) du stator interne (22) contigu au dispositif de séparation (32) et un dispositif de dérivation (62).
  10. Broyeur à agitateur selon la revendication 9, caractérisé en ce que le dispositif de dérivation (62) est un composant autonome de l'agitateur (20).
  11. Broyeur à agitateur selon la revendication 8, caractérisé en ce que l'interstice j du canal d'écoulement (59) s'élargit en direction du dispositif de (32).
  12. Broyeur à agitateur selon l'une des revendications 8 à 11, caractérisé en ce que le stator interne (22) est équipé d'un anti abrasif (63) au niveau du canal d'écoulement (59).
  13. Broyeur à agitateur selon l'une des revendications 1 à 12, caractérisé en ce que les canaux de retour de corps auxiliaires d'aliments (54) sont disposés dans un module de retour de corps auxiliaires d'aliments (45) autonome.
  14. Broyeur à agitateur selon la revendication 13, caractérisé en ce que les canaux de retour de corps auxiliaires d'aliments (54) sont ouverts sur un front (67) du module de retour (45).
  15. Broyeur à agitateur selon l'une des revendications 1 à 14, caractérisé en ce que les canaux de retour (54) présentent une ouverture d'entrée (55) d'une dimension c et une ouverture de sortie (56) d'une dimension d
    et en ce que pour la dimension c de l'ouverture d'entrée (55) par rapport à la dimension d de l'ouverture de sortie (56), on a :
    d > c et de préférence
    d ≥ 1,5 c.
  16. Broyeur à agitateur selon l'une des revendications 1 à 15, caractérisé en ce que en direction de l'axe central (19), les canaux de retour de corps auxiliaires d'aliments (54) présentent une hauteur e et le dispositif de séparation des corps auxiliaires d'aliments (32) une hauteur f et
    en ce que pour la hauteur e par rapport à la hauteur f, on a :
    e ≤ f et de préférence
    e < 0,5 f.
  17. Broyeur à agitateur selon les revendications 13 à 16, caractérisé en ce que le module de retour (45) contigu au dispositif de séparation (32) est équipé de racleurs (65) qui passent en continu, sans interruption dans les canaux de retour (54).
  18. Broyeur à agitateur selon la revendication 17, caractérisé en ce que les racleurs (65) s'étendent sur la hauteur f du dispositif de séparation de corps auxiliaires d'aliments (32)
EP05010815A 2005-05-19 2005-05-19 Broyeur à agitateur Not-in-force EP1724022B1 (fr)

Priority Applications (8)

Application Number Priority Date Filing Date Title
ES05010815T ES2285603T3 (es) 2005-05-19 2005-05-19 Molino agitador.
DE502005000670T DE502005000670D1 (de) 2005-05-19 2005-05-19 Rührwerksmühle
EP05010815A EP1724022B1 (fr) 2005-05-19 2005-05-19 Broyeur à agitateur
AT05010815T ATE361146T1 (de) 2005-05-19 2005-05-19 Rührwerksmühle
US11/171,319 US7216822B2 (en) 2005-05-19 2005-07-01 Agitator mill
JP2006138920A JP5010853B2 (ja) 2005-05-19 2006-05-18 撹拌機ミル
KR1020060044818A KR101245478B1 (ko) 2005-05-19 2006-05-18 교반기 밀
CNB2006100826375A CN100544892C (zh) 2005-05-19 2006-05-19 搅拌设备

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
EP05010815A EP1724022B1 (fr) 2005-05-19 2005-05-19 Broyeur à agitateur

Publications (2)

Publication Number Publication Date
EP1724022A1 EP1724022A1 (fr) 2006-11-22
EP1724022B1 true EP1724022B1 (fr) 2007-05-02

Family

ID=34936667

Family Applications (1)

Application Number Title Priority Date Filing Date
EP05010815A Not-in-force EP1724022B1 (fr) 2005-05-19 2005-05-19 Broyeur à agitateur

Country Status (8)

Country Link
US (1) US7216822B2 (fr)
EP (1) EP1724022B1 (fr)
JP (1) JP5010853B2 (fr)
KR (1) KR101245478B1 (fr)
CN (1) CN100544892C (fr)
AT (1) ATE361146T1 (fr)
DE (1) DE502005000670D1 (fr)
ES (1) ES2285603T3 (fr)

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EP4032615A1 (fr) 2021-01-25 2022-07-27 Wilhelm Niemann GmbH & Co KG Broyeur agitateur

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US20090212141A1 (en) * 2005-06-08 2009-08-27 Alan Taylor Milling apparatus
EP2327480A1 (fr) * 2009-11-25 2011-06-01 Willy A. Bachofen AG Broyeur à billes à agitateur
CN102814217A (zh) * 2012-08-31 2012-12-12 常州市龙鑫化工机械有限公司 一种高效再循环珠磨机
CN109746088A (zh) * 2017-11-08 2019-05-14 深圳市微纳达智能设备有限公司 一种立式封闭无机械密封管网出料介质搅拌磨
IT201800003874A1 (it) * 2018-03-22 2019-09-22 Certech Spa Con Socio Unico Mulino per materiali ceramici
EP3650123A1 (fr) * 2018-11-09 2020-05-13 Bühler AG Broyeur à passage annulaire
CN110900822B (zh) * 2019-11-08 2021-08-24 南京赛诺特斯材料科技有限公司 一种改善氧化锆粉体陶瓷性能的复合添加剂
JP7454066B2 (ja) * 2020-03-27 2024-03-21 ビューラー アーゲー アジテータボールミル

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DE29814714U1 (de) * 1998-08-17 1998-12-10 Draiswerke Gmbh, 68305 Mannheim Rührwerksmühle
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JP4451965B2 (ja) * 2000-05-18 2010-04-14 株式会社井上製作所 パイプラインビ−ズミル
JP2002204969A (ja) 2001-01-10 2002-07-23 Inoue Seisakusho:Kk パイプラインビ−ズミル
JP4268445B2 (ja) * 2002-05-17 2009-05-27 株式会社日清製粉グループ本社 機械式粉砕装置

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP4032615A1 (fr) 2021-01-25 2022-07-27 Wilhelm Niemann GmbH & Co KG Broyeur agitateur
DE102021101527A1 (de) 2021-01-25 2022-07-28 Wilhelm Niemann Gmbh & Co. Rührwerksmühle
DE102021101527B4 (de) 2021-01-25 2023-05-17 Wilhelm Niemann Gmbh & Co. Rührwerksmühle

Also Published As

Publication number Publication date
CN1864928A (zh) 2006-11-22
ES2285603T3 (es) 2007-11-16
US20060261200A1 (en) 2006-11-23
ATE361146T1 (de) 2007-05-15
EP1724022A1 (fr) 2006-11-22
CN100544892C (zh) 2009-09-30
US7216822B2 (en) 2007-05-15
DE502005000670D1 (de) 2007-06-14
JP2006320898A (ja) 2006-11-30
KR101245478B1 (ko) 2013-03-25
JP5010853B2 (ja) 2012-08-29
KR20060120465A (ko) 2006-11-27

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