EP2905080A1 - Broyeur à billes à agitateur - Google Patents

Broyeur à billes à agitateur Download PDF

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Publication number
EP2905080A1
EP2905080A1 EP14154350.4A EP14154350A EP2905080A1 EP 2905080 A1 EP2905080 A1 EP 2905080A1 EP 14154350 A EP14154350 A EP 14154350A EP 2905080 A1 EP2905080 A1 EP 2905080A1
Authority
EP
European Patent Office
Prior art keywords
chamber
stirring
agitator
ball mill
return
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.)
Ceased
Application number
EP14154350.4A
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German (de)
English (en)
Inventor
Erfindernennung liegt noch nicht vor Die
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.)
Willy A Bachofen AG
Original Assignee
Willy A Bachofen 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
Application filed by Willy A Bachofen AG filed Critical Willy A Bachofen AG
Priority to EP14154350.4A priority Critical patent/EP2905080A1/fr
Priority to ES15702511.5T priority patent/ES2669612T3/es
Priority to PCT/EP2015/052463 priority patent/WO2015118090A1/fr
Priority to MYPI2016702553A priority patent/MY180354A/en
Priority to KR1020167024585A priority patent/KR102385148B1/ko
Priority to US15/116,381 priority patent/US10464069B2/en
Priority to PL15702511T priority patent/PL3102332T3/pl
Priority to DK15702511.5T priority patent/DK3102332T3/en
Priority to JP2016550816A priority patent/JP6734195B2/ja
Priority to CN201580007622.XA priority patent/CN106061613B/zh
Priority to EP15702511.5A priority patent/EP3102332B1/fr
Publication of EP2905080A1 publication Critical patent/EP2905080A1/fr
Ceased legal-status Critical Current

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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
    • B02C17/163—Stirring means
    • 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
    • B02C17/16—Mills in which a fixed container houses stirring means tumbling the charge
    • B02C17/161—Arrangements for separating milling media and ground material
    • 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
    • B02C17/168—Mills in which a fixed container houses stirring means tumbling the charge with a basket media milling device arranged in or on the container, involving therein a circulatory flow of the material to be milled
    • 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
    • B02C17/20—Disintegrating members
    • 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
    • B02C2017/165—Mills in which a fixed container houses stirring means tumbling the charge with stirring means comprising more than one agitator

Definitions

  • the present invention relates to a stirred ball mill according to the independent claim.
  • An agitator ball mill of the generic type is eg in WO 2010/112274 described.
  • the agitator ball mill described therein comprises a substantially cylindrical grinding chamber, which is delimited by a jacket and one inlet and one outlet end wall, and a rotatably mounted stirring shaft, on the inside of the grinding chamber paddle wheel-like, also referred to as accelerators stirring members are arranged axially mutually spaced , In the vicinity of the inlet-side end wall, an inlet for supplying ground material and grinding bodies is arranged and in the outlet-side end wall, an outlet for removing the ground Guts is provided, which is separated by a grinding medium-retaining separator screen from the grinding chamber.
  • the agitator shaft and thus the non-rotatably connected stirrers are rotated by an external motor in rotation.
  • Agitator ball mills of similar construction are, for example, in EP 0 627 262 and EP 2 272 591 described.
  • agitator ball mills equipped with paddle-wheel agitators, convey during the grinding and / or dispersing process a portion of the mixture formed from grinding media and the material to be ground and / or dispersed radially outwardly, whereupon at least a portion of the mixture is directed towards the stirring shaft and from there back into the Delivery chambers of the stirring elements flows or is sucked.
  • MahlSystemnikank This process is referred to below as MahlSystemnikank.
  • the present invention is an agitator ball mill of the generic type to be improved so that the grinding media can not or at most only accumulate to a greatly reduced extent at the periphery of the grinding chamber, but as completely entrained from being ground and / or to be dispersed Good and so MahlSystemnikank be supplied.
  • the agitator ball mill comprises a grinding chamber, a rotatably mounted agitating shaft projecting at least partially into the grinding chamber, on which stirring elements are axially spaced apart within the grinding chamber, and an inlet for supplying ground material and grinding bodies and an outlet for removing the ground material ,
  • the stirring members each have at least one delivery chamber and are formed so that they in operation from a to be milled or to be dispersed Good and grinding media existing mixture through its at least one delivery chamber through the agitator shaft away to the outside, and wherein in the grinding chamber with the agitator shaft rotatably connected mulch pieceorgane are arranged, which promote the mixture laterally next to and / or between the Rix inwardly to the agitator shaft during operation.
  • through in this context means that the material to be ground or to be dispersed is conveyed away from the agitator shaft into the delivery chamber, outward in the delivery chamber, and then out of the delivery chamber.
  • the return conveyors produce a flow field directed inwardly toward the agitator shaft, which increases the drag forces of the material to be ground and / or dispersed. Grinding media, which come into contact with these posts officeorganen receive a likewise directed inward to the agitator shaft pulse. Both support the maintenance of the desired Mahl stressesnikanks.
  • the return means are arranged laterally on the stirring elements.
  • “Laterally” means that the return devices are arranged on those sides of the stirring elements, which point in the direction of the axis of rotation of the agitator shaft (the axis of rotation of the agitator shaft is therefore perpendicular to these sides), for example, the remindicaorgane of lateral end faces of the stirring elements from.
  • the return-conveying elements are arranged at a distance laterally next to and / or between the stirring elements. Both aspects are structurally particularly favorable.
  • the return-conveying elements are arranged laterally on at least one separate (preferably disk-shaped) support which is connected in a rotationally fixed manner to the agitator shaft.
  • the return means are designed as return feed vanes.
  • the stirring elements according to a further aspect may be formed as paddle wheels and having steering blades, which are employed obliquely inwardly from the outside in the direction of rotation of the stirring elements and are preferably curved in the direction of rotation of the stirring members, wherein the return blades against the direction of rotation of the stirring elements obliquely inwards are employed.
  • the return feed vanes are arranged in at least one return conveyor unit which is connected in a rotationally fixed manner to the agitator shaft and is designed as a paddle wheel.
  • the return feed vanes are curved in the direction of rotation.
  • the radius of curvature of the return flow blades can be, for example, 40% -70% of the outer diameter of the stirring elements.
  • the return feed vanes each have an inner end and an outer end, wherein the return feed vanes enclose at their inner end an angle with the circumferential direction at the location of the respective inner end, which is in the range of 5 ° to 30 ° ,
  • the stirring elements arranged on the agitator shaft are designed as single-chamber agitators and / or two-chamber agitators and each have an equal outer diameter, the distance between a one-chamber agitator and an adjacently disposed single chamber agitator or between a one-chamber stirrer and an adjacent two-chamber impeller in the range of 10% -20% of the outer diameter of the stirrers, and wherein the distance between a two-chamber -Rownorgan and an adjacently arranged two-chamber stirring member in the range of 30% - 40% of the outer diameter of the stirring elements. This further optimizes the media circulation.
  • the agitating ball mill comprises a grinding chamber, a rotatably mounted agitating shaft projecting at least partially into the grinding chamber, on which stirring elements are axially spaced apart within the grinding chamber, and an inlet for supplying ground material and grinding bodies and an outlet for removing the ground material, wherein the stirring elements each have at least one delivery chamber and are designed such that during operation they convey a mixture consisting of material to be milled or dispersed and grinding bodies outwardly away from the agitator shaft through their at least one delivery chamber, wherein the arranged on the agitator stirrer agitators are designed as a one-chamber stirrers and / or as a two-chamber stirring members and each having an equal outer diameter, wherein the distance between a one-chamber stirrer and an adjacent angeor dneten one-chamber agitator or between a one-chamber stirrer and an adjacently arranged two-chamber agitator in the range of 10% -
  • the problem underlying the invention of the accumulation of grinding media in the Mahlhuntperipherie is solved by the special mutual arrangement of Rlochorgane, whereby the grinding media entrained to be ground and / or to be dispersed Good and fed to the grinding body cycle.
  • the return devices are arranged laterally on the stirring elements.
  • the return means are arranged at a distance laterally next to and / or between the stirring members.
  • the return-conveying elements are arranged laterally on at least one separate (preferably disk-shaped) support which is connected in a rotationally fixed manner to the agitator shaft.
  • the return devices are designed as return feed vanes.
  • the stirring elements are formed as paddle wheels and have steering vanes, which are employed obliquely inwardly in the direction of rotation of the stirring elements inwardly and are preferably formed curved in the direction of rotation of the stirring elements, wherein the return blades from the outside against the direction of rotation of the stirring elements obliquely inwards are employed.
  • the return-conveying blades are arranged in at least one return-conveying unit which is connected in a rotationally fixed manner to the agitating shaft and designed as a paddle wheel.
  • the return feed vanes are curved in the direction of rotation.
  • the radius of curvature of the return flow blades can be, for example, 40% -70% of the outer diameter of the stirring elements.
  • the return feed vanes each have an inner end and an outer end, wherein the return feed vanes enclose at their respective inner ends with the circumferential direction at the location of the respective inner end an angle which is in the range of 5 ° to 30 °.
  • the agitator ball mill comprises a substantially cylindrical grinding chamber 1, which is bounded by a jacket 2 and each one inlet and one outlet-side end wall 3 and 4 respectively.
  • a substantially cylindrical grinding chamber 1 which is bounded by a jacket 2 and each one inlet and one outlet-side end wall 3 and 4 respectively.
  • an externally or in the end wall rotatably mounted agitator shaft 5 is carried out on the inside of the grinding chamber 1, three paddle wheel-like agitators or accelerators 10, 20 and 30 are arranged axially spaced from each other.
  • the accelerators 10, 20 and 30 are rotatably connected to the agitator shaft and are rotationally driven during operation thereof.
  • an inlet 6 for the supply of ground material and grinding media is arranged and in the outlet-side end wall 4, an outlet 7 is provided for removing the ground material, the outlet 7 by a the grinding media retaining separator screen 8 of the Grinding chamber 1 is separated.
  • an open towards the interior of the grinding chamber 1 annular channel 9 is formed.
  • the accelerator 10 hereinafter referred to as a single-chamber accelerator comprises two parallel annular disks 11 and 12, between which are arranged curved steering vanes 14 which extend obliquely inwards from the outer circumference of the disks in the direction of rotation P.
  • the disk 12 is provided close to the stirring shaft with a series of openings 15 through which the mixture of grinding stock and grinding media can enter the accelerator 10.
  • the openings 15 can also be guided at an angle of 40 ° - 50 ° to Rhakwellenachse or slotted.
  • the disc 11 has a diameter in the relatively large central opening 16 ( Fig. 1 ) serving the same purpose (entry of the mixture into the accelerator).
  • the two annular disks 11 and 12 define between them a delivery chamber and together with the steering vanes 14 form a single-chamber impeller, which upon rotation of the agitator shaft 5 (FIG. Fig. 1 ) and thus of the accelerator 10 in the direction of rotation P, the mixture in the delivery chamber of grinding stock and grinding media to the outside in the direction of the periphery (shell 2) of the grinding chamber 1 promotes.
  • the accelerator 20 differs from the accelerator 10 by training as a two-chamber accelerator. It comprises three parallel annular discs 21, 22 and 23, between each of which curved steering vanes 24 are arranged, which extend obliquely inwardly from the outer circumference of the discs in the direction of rotation P.
  • the middle disc 23 forms the supporting element and is rotatably mounted on the agitator shaft 5.
  • the middle disc 23 is further provided Rfordwellennah with a series of openings 25 through which the mixture of regrind and grinding media can pass.
  • the openings 25 can also be guided at an angle of 40 ° - 50 ° to Rhakwellenachse or slotted.
  • the two outer discs 21 and 22 each have a diameter in the relatively large central opening 26 through which the mixture of grinding stock and grinding media can enter the accelerator 20.
  • the three annular disks 21, 22, 23 define between them two delivery chambers and together with the steering vanes 24 form a two-chamber impeller, which upon rotation of the agitator shaft 5 (FIGS. Fig. 1 ) and thus of the two-chamber accelerator 20 in the direction of rotation P located in the delivery chambers mixture of regrind and Grinding bodies to the outside in the direction of the periphery (shell 2) of the grinding chamber 1 promotes.
  • the accelerator 30, which is referred to below as a two-chamber end accelerator, is in principle designed in the same way as the two-chamber accelerator 20. It comprises two annular outer disks 31 and 32 and a middle disk 33, between each of which curved steering blades 34 are arranged are that extend obliquely inward from the outer circumference of the discs in the direction of rotation P.
  • the two-chamber end accelerator 30 is attached to the free end of the agitator shaft 5, with its central disc 33 screwed to the end of the agitator shaft.
  • the middle disc 33 could also be formed similar to the middle disc 23 of the accelerator 20 and mounted on the stirrer shaft.
  • the middle disc 33 is again provided with a series of openings 35 close to the stirring shaft, and the two outer discs 31 and 32 each have a diameter opening which is relatively large in diameter.
  • the openings 35 can also be guided at an angle of 40 ° - 50 ° to the stirrer shaft axis or slotted.
  • the three discs 31, 32, 33 define between them two delivery chambers and form together with the steering vanes 34 again a two-chamber paddle wheel, although the guide vanes between the central disc 33 and the outlet 7 facing outer disc 33 in the axial direction wider are the steering vanes between the middle disc 33 and the other outer disc 31.
  • the two-chamber end accelerator 30 engages with its wider steering paddles the separator screen 8 Fig. 1 ).
  • Fig. 1 and also in the FIGS. 7 and 11-13 are some typical mass of the grinding chamber 1 and the accelerators 10, 20 and 30 registered.
  • the inner diameter of the grinding chamber 1 or of the jacket 2 is denoted by D.
  • D a is the external diameter (normally the same for all accelerators) of the accelerators 10, 20 and 30. It is typically 75% -90% of the grinding chamber diameter D.
  • the mass d i denotes the diameter (usually the same for all accelerators) of the central openings 16, 26 and 36 of the accelerators 10, 20 and 30. It is typically 70% -80%. of the outer diameter d a .
  • c1, c2 and c3 are measured in the axial direction Total widths of the accelerators 10, 20 and 30 are designated.
  • the dimension k designates the delivery chamber widths of the accelerators 10, 20 and 30 defined by the inner spacing of two respective adjacent disks 11, 12 and 21, 23 and 23, 22 and 31, 33 of the accelerators 10, 20 and 30. They are typically 5% - 15% of the outer diameter d a . With a, the axial distance of the inlet-side end wall 3 nearest accelerator is designated by the end wall. It is typically 10% - 15% of the outer diameter d a .
  • the masses b1 and b2 denote the axial distances between adjacent accelerators. The distances b1 and b2 between the accelerators 10, 20 and 30 will be discussed in more detail below.
  • the mixture consisting of material to be milled or dispersed occurs and enters the accelerators or stirrers 10, 20 and 30 through the openings near the stirrer shaft 16 or 26 or 36 and passes through their delivery chamber or delivery chambers from the accelerators or stirrers out to the outside in the peripheral or jacket-near area of the grinding chamber 1 promoted. From there, a part of the mixture flows in the already mentioned MahlSystemnikank laterally next to and between the accelerators back into the R industrialwellennahen area and is sucked from there back into the accelerators. The ground or dispersed material is discharged through the outlet 7 from the grinding chamber.
  • the openings 15 and 25 or 35 serve to compensate for an axial Mahl emotionsfall.
  • these return conveyors are arranged laterally on one or both of the outer disks 11 or 21 and 22 or 31 of the accelerators 10, 20 and 30 (they stand from the respective lateral end faces of the outer disks 11 and 21 in the direction of the axis of rotation of the agitator shaft ab) and are denoted there by 17, 27 and 37.
  • the detailed representation of the Fig. 5 which the accelerator 20 of the Fig. 1 shows isolated in perspective oblique view, can clearly recognize the shape and arrangement of the return conveyor 27.
  • each of the two outer annular discs 21 and 22 of the accelerator 20 are each four in the direction of rotation P of the accelerator 20 curved return conveyors in the form of return feed vanes 27 are arranged.
  • the return feed vanes 27 are in principle similar to the steering vanes 24 of the accelerator 20, but employed opposite in relation to the direction of rotation so that they unfold a conveying effect in reverse direction upon rotation of the accelerator 20 in the direction of rotation P, ie from outside to inside in the direction towards the agitator shaft.
  • the number of return feed vanes 27 per side of the accelerator 20 may also be less than or greater than four, for example, up to twenty.
  • the return conveyors are also formed as return feed vanes 17 and 37 and arranged the same as in the accelerator 20, but here in the embodiment only on one side of the accelerator 10 and 30.
  • the number of return feed vanes can also be smaller or larger be four and for example also up to twenty.
  • the height h of the return feed vanes 17, 27 and 37 measured in the axial direction is approximately 5% to 15% of the outer diameter d a of the accelerators 10, 20 and 30 (FIG. Fig. 1 ).
  • the radius of curvature r s of the return feed vanes 17, 27 and 37 is preferably about 40% - 70% of the outer diameter d a ( Fig. 1 ) of the accelerators 10, 20 and 30 ( Fig. 6 ).
  • the angle of attack ⁇ enclosed between the circumferential direction t u at the location of the inner ends 27i of the return feed vanes 17, 27 and 37 and the tangent t s at the inner ends of the return feed vanes is approximately 5 ° -30 ° (FIG. Fig. 6 ).
  • the return feed vanes 17, 27 and 37 on the one hand, generate a flow field directed inwards towards the stirrer shaft, which increases the drag forces of the material to be ground and / or to be dispersed.
  • grinding bodies which come into contact with these return-conveying blades also receive an impulse directed inwards towards the stirring shaft. Both support the maintenance of the desired Mahl stressesnikanks.
  • Fig. 7 is a second embodiment of the inventive agitator ball mill shown.
  • a first difference compared to the embodiment of Fig. 1 is that on the agitator 5, instead of the single-chamber accelerator 10, a further two-chamber accelerator 20 is arranged on the agitator shaft.
  • the return devices are not arranged on the stirrers or accelerators 20 and 30, but are designed as separate return conveyor units 40 and preferably arranged centrally between two accelerators.
  • Fig. 8 shows the formation of such a return unit 40 in a perspective oblique view. It consists of a disc-shaped carrier 41 and four each arranged on both sides of the carrier return conveyor blades 47.
  • the carrier 41 is on the agitator shaft 5 (FIG. Fig. 6 ) and rotatably connected thereto.
  • the carrier 41 in the Rhackwellennahen area a number of openings 45 through which the millbase / grinding media mixture can flow through.
  • the openings 45 can also be performed at an angle of 40 ° - 50 ° to Rhakwellenachse or slotted.
  • Arrangement, training and number the return feed vanes 47 are the same as in connection with Fig. 5 and Fig. 6 therefore, they do not explain and need no further explanation.
  • FIGS. 9 and 10 show a third embodiment of the inventive agitator ball mill.
  • two two-chamber accelerators 20 and a two-chamber-end accelerator 30 are arranged, all of which are also not equipped with return feed vanes.
  • a return conveyor unit 50 designed as a two-chamber impeller is arranged between two adjacent ones of the three accelerators.
  • the return conveyor units 50 are in principle the same design as the Schaufelradartigen two-chamber accelerators 20. They therefore have three annular discs 51, 52 and 53 and in each case between these curved and obliquely inwardly employed return conveyor blades 57 on.
  • the middle disc 53 is fixedly mounted on the agitator shaft 5 and has in its RZwellennahen area a number of through openings, not shown. The openings can also be guided at an angle of 40 ° - 50 ° to Rrockwellenachse or slotted.
  • the two outer discs 51 and 52 each have a diameter in the relatively large central opening 56.
  • the discs 51, 53 and the discs 52, 53 each define a delivery chamber, a total of two delivery chambers, and together with the return feeders 57 form a two-chamber paddle wheel analogous to the two-chamber accelerator 20, but with conveying direction from outside to inside instead of inside out.
  • the return conveyor unit 50 could also be realized by a two-chamber accelerator 20 mounted on the agitator shaft 5 "oriented upside down". With regard to the shape, arrangement and number of return feed vanes 57, the same considerations apply as stated in connection with the first two embodiments.
  • the return conveyor units 50 can be arranged between the individual accelerators at an axial distance from the accelerators or preferably completely between the accelerators, which then results in a particularly compact design.
  • FIGS. 11-13 three further embodiments of the inventive agitator mill are each shown in an axial section.
  • Each of the three embodiments comprises a substantially cylindrical grinding chamber 1 which is delimited by a jacket 2 and an inlet and an outlet-side end wall 3 and 4, respectively.
  • an agitator shaft 5 which is rotatably mounted externally or in the end wall is carried out, on which agitator-type stirring elements or accelerators are arranged axially at a mutual distance within the grinding chamber 1.
  • the accelerators are rotatably connected to the agitator shaft and are rotationally driven during operation.
  • an inlet 6 for supplying grinding stock and grinding media is arranged, and in the outlet-side end wall 4 is provided an outlet 7 for removing the ground product, which is separated from the grinding chamber 1 by a grinding medium-retaining separator screen 8 , In the outlet-side end wall 4, an open towards the interior of the grinding chamber 1 annular channel 9 is formed.
  • the agitator ball mill of Fig. 11 corresponds in principle to that of Fig. 7 and comprises two two-chamber accelerators 20 and a two-chamber end accelerator 30.
  • the agitator ball mill of Fig. 12 includes three single-chamber accelerators 10 and a two-chamber final accelerator 30.
  • the agitator ball mill of Fig. 13 corresponds in principle to that of Fig. 1 and includes a single-chamber accelerator 10, a two-chamber accelerator 20, and a two-chamber end accelerator 30.
  • the accelerators 10, 20, and 30 are as in FIG Related to the Figures 2-4 described trained and therefore require no further explanation.
  • the ratio is chosen so that the distance traveled by the grinding media is so long that they can deliver sufficient kinetic energy on their way, so that the resulting inertial forces are less than the drag forces of the material to be ground and / or to be dispersed ,
  • this "calming distance” is chosen to be sufficiently short so that the kinetic energy maintains a sufficiently high level in order to maintain the desired intensive mechanical stress of the material to be ground and / or dispersed.
  • the required ratio between the defined by the channel width k free volume within an accelerator to the volume defined by the distance between two adjacent accelerators is realized according to the invention by a special dimensioning of the distances b1 and b2 between the accelerators.
  • the distances b1 between each two of the one-chamber accelerators 10 and the distance b1 between the third single-chamber accelerator 10 and the two-chamber end accelerator 30 are in the range of 10% - 20% of the outer diameter d a Accelerators 10 and 30.
  • Fig. 13 are the distance b1 between the one-chamber accelerator 10 and the adjacent two-chamber accelerator 20 in the range of 10% - 20% of the outer diameter d a of the accelerators 10, 20 and 30 and the distance b2 between the two-chamber -Accelerator 20 and the two-chamber-end accelerator 30 in the range of 30% - 40% of the outer diameter d a of the accelerators 10, 20 and 30.
  • the described dimensioning of the distances between the accelerators 10, 20 and 30 can also be advantageous in the embodiments equipped with return means according to the FIGS. 1 and 7 be applied.
  • the distances b1 and b2 are also entered in these figures.
  • the optimized enlargement of the distances between the accelerators according to the above design rule leads in combination with the Use of recirculation means to further improve the grinding media cycle.

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  • Engineering & Computer Science (AREA)
  • Food Science & Technology (AREA)
  • Crushing And Grinding (AREA)
  • Mixers Of The Rotary Stirring Type (AREA)
EP14154350.4A 2014-02-07 2014-02-07 Broyeur à billes à agitateur Ceased EP2905080A1 (fr)

Priority Applications (11)

Application Number Priority Date Filing Date Title
EP14154350.4A EP2905080A1 (fr) 2014-02-07 2014-02-07 Broyeur à billes à agitateur
ES15702511.5T ES2669612T3 (es) 2014-02-07 2015-02-06 Molino de bolas con agitador
PCT/EP2015/052463 WO2015118090A1 (fr) 2014-02-07 2015-02-06 Broyeur-agitateur à billes
MYPI2016702553A MY180354A (en) 2014-02-07 2015-02-06 Agitator ball mill
KR1020167024585A KR102385148B1 (ko) 2014-02-07 2015-02-06 교반기 볼 밀
US15/116,381 US10464069B2 (en) 2014-02-07 2015-02-06 Agitator ball mill
PL15702511T PL3102332T3 (pl) 2014-02-07 2015-02-06 Młyn kulowy mieszalnika
DK15702511.5T DK3102332T3 (en) 2014-02-07 2015-02-06 Agitator ball mill
JP2016550816A JP6734195B2 (ja) 2014-02-07 2015-02-06 攪拌ボールミル
CN201580007622.XA CN106061613B (zh) 2014-02-07 2015-02-06 搅拌球磨机
EP15702511.5A EP3102332B1 (fr) 2014-02-07 2015-02-06 Broyeur à billes à agitateur

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
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US10518269B2 (en) 2017-10-13 2019-12-31 SPEX SamplePrep, LLC Grinding mill with securing frame
CN109046697A (zh) * 2018-09-21 2018-12-21 广州鸿凯机械科技有限公司 研磨机构、分散研磨装置及分散研磨***
CN112024060A (zh) * 2020-09-18 2020-12-04 广州京驰精工机械设备有限公司 一种大流量动态防堵分离***
CN114534866A (zh) 2020-11-18 2022-05-27 威利A.巴霍芬公司 搅拌式球磨机
CN114178002B (zh) * 2021-11-08 2023-05-09 北京天地融创科技股份有限公司 细磨机

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EP0627262A1 (fr) 1993-06-01 1994-12-07 Willy A. Bachofen AG Broyeur agitateur à billes travaillant en continu pour le broyage fin et ultrafin de matériaux
EP0627262B1 (fr) 1993-06-01 1999-03-24 Willy A. Bachofen AG Broyeur agitateur à billes travaillant en continu pour le broyage fin et ultrafin de matériaux
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EP3311922A1 (fr) * 2016-10-18 2018-04-25 Willy A. Bachofen AG Broyeur à billes à agitateur
US10792665B2 (en) 2016-10-18 2020-10-06 Willy A. Bachofen Ag Agitator ball mill

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KR20160117601A (ko) 2016-10-10
PL3102332T3 (pl) 2018-09-28
US10464069B2 (en) 2019-11-05
JP6734195B2 (ja) 2020-08-05
WO2015118090A1 (fr) 2015-08-13
CN106061613B (zh) 2018-12-11
JP2017505228A (ja) 2017-02-16
EP3102332B1 (fr) 2018-03-28
CN106061613A (zh) 2016-10-26
EP3102332A1 (fr) 2016-12-14
US20170014830A1 (en) 2017-01-19
KR102385148B1 (ko) 2022-04-11
MY180354A (en) 2020-11-28
DK3102332T3 (en) 2018-07-02
ES2669612T3 (es) 2018-05-28

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