Title of Invention

AGITATING BALL MILL

Abstract Agitating ball mill with a cylindrical grinding vessel (26) comprising at least one grinding stock inlet (24) and at least one grinding stock outlet (34) wherein in the grinding vessel (26) an agitating shaft (20) connected with a drive (12) is arranged which transmits a part of the drive energy to auxiliary grinding bodies (54) which are loosely arranged in the grinding vessel (26) and a separating device (30) arranged in front of the grinding vessel outlet (34).
Full Text Agitating ball mill
The invention relates to an agitating ball mill with a cylindrical grinding vessel having
10 at least one grinding stock inlet and at least one grinding stock outlet, wherein in the
grinding stock vessel an agitating shaft connected with a drive is arranged which
transmits a part of the drive energy to auxiliary grinding bodies which are loosely
arranged in the grinding vessel and a separating device arranged in front of the grinding
stock outlet.
15
An agitating ball mill of this kind emerges from EP 1 468 739 Al. With this
horizontally arranged agitating mill the grinding vessel is in connection with a grinding
stock inlet and a grinding stock outlet. In the grinding vessel proper is located an
agitating shaft which is in connection with a drive. The auxiliary grinding bodies filled
20 into the grinding chamber are accelerated through agitating organs so that the grinding
stock located between the auxiliary grinding bodies is ground or dispersed. The fineness
of the product produced in this agitating ball mill is largely dependent on the size of the
auxiliary grinding bodies employed. To separate the auxiliary grinding bodies from the
grinding stock a separating device connected with the grinding stock outlet is provided
25 at the end of the grinding vessel. This separating device comprises several arc-shaped
conveying or wing elements which are arranged between two discs. The wing elements
extend from the outer edge of the discs in the direction of their centre, wherein the
elements partly end at different distances from the grinding stock outlet.
30 Because of the short distance which the auxiliary grinding bodies have to cover between
the wing elements entry of auxiliary grinding bodies in the grinding outlet while the
separating device is stationary cannot be prevented.
The object of the invention therefore consists in improving a separating device also for
35 smallest grinding bodies so that entry of the auxiliary grinding bodies in the grinding
stock outlet is prevented even during the start-up and run-down phase of the agitating
ball mill. This object is solved with the characteristics of Claim 1.

5 Further embodiments according to the invention are mentioned in the characteristics of
the subclaims.
Through the invention an agitating ball mill is thus created with a cylindrical grinding
vessel having at least one grinding stock inlet and one grinding stock outlet, wherein the
10 grinding vessel arranged horizontally as shown in the exemplary embodiment has an
agitating shaft connected with a drive which transmits a part of the drive energy to the
auxiliary grinding bodies. To separate the auxiliary grinding bodies from the grinding
stock a separating device is employed which comprises at least one spiral.
15 With a preferred embodiment employed with smallest grinding bodies the separating
device consists of two spirals.
A further preferential embodiment provides that the spirals are arranged with a constant
distance to each other.
20
With smallest grinding bodies it can be advantageous to arrange the spirals with a
varying distance to each other.
Another preferential embodiment of the invention is provided in order to achieve that
25 the auxiliary grinding bodies among themselves are retained by friction. Here, the spiral
directly extends with its radially inner end as far as the grinding stock outlet.
In order to increase the throughput in the agitating ball mill the grinding stock outlet can
extend on both sides of the longitudinal centre of the spiral.
30
It has been shown that secure separation of the auxiliary grinding bodies from the
grinding stock takes place when the spiral/s extend/s by a circumference of at least 360°
about the longitudinal axis of the agitating shaft.
35 Depending on the throughput with which the mill is operated it can be advantageous if
the width of the spiral/s amounts to at least one third of its diameter.

5 Since the spiral/s guarantee/s secure separation of the auxiliary grinding bodies from the
grinding stock even with few revolutions it can be advantageous to rotate the spiral/s via
an independent drive.
According to an advantageous arrangement in which the spiral/s is/are protected against
10 excessive wear at the outer end the spiral sits between the agitating shaft surface and the
longitudinal axis of the agitating shaft. Within a cage-like section of the agitating shaft
which in this region comprises radial openings.
In order to promote the outflow of the auxiliary grinding bodies in this cage-like region
15 the slot-shaped openings are inclined contrary to the direction of rotation of the
agitating shaft.
Depending on the viscosity values which the product has it can be an advantage to
configure the openings of the agitating shaft tangentially or asymmetrically to the
20 longitudinal axis of the latter.
To loosen up the auxiliary grinding body package in the region of the outlet it can be an
advantage to provide the agitating shaft with agitating elements in the region of the
spiral/s which consist of agitating bars or cleats and which are staggered by at least 45°
25 relative to one another.
With a further preferential embodiment the spiral/s contrary to the normal embodiment
in which it/they consist/s of plate, consist/s of bars and webs individually spaced from
one another. However, these bars and webs need not be connected with one another in a
30 contacting manner.
It is further preferred that the diameter of the spiral/s comprises at least 30% of the
grinding chamber diameter.
35 In a further embodiment version the diameter of the spiral/s is at least 30% of the
diameter of the hollow space in the agitating shaft.

5 If the separating device is employed with a drive arranged independently from the
agitating shaft it can be an advantage if the spirals are inserted between two holohedral
end faces.
To improve the backflow of the auxiliary grinding bodies it can be an advantage if the
10 end faces located laterally on the spirals comprise openings through which the auxiliary
grinding bodies can flow back into the grinding chamber.
To influence the flow direction in the region of the outlet it will be an advantage if a
laterally arranged displacement body is inserted in the spiral/s.
15
The invention is explained in more detail merely exemplarily in the following by means
of exemplary embodiments making reference to the drawings. It shows:
Figure 1 schematic lateral view of an agitating ball mill
20 Figure 2 schematic lateral view of the ball mill
Figure 3 vertical section to a spiral arrangement
Figure 4 vertical section through a screw guideway
Figure 5 part view of the agitating shaft with spiral section
Figure 6 vertical section of the agitating shaft
25 Figure 7 schematic lateral view of an agitating ball mill
Figure 8 schematic lateral view of an agitating ball mill
Figure 9 vertical section through an agitating shaft
Figure 10 vertical section through an agitating shaft
Figure 11 schematic lateral view of a grinding vessel
30 Figure 12 vertical section of an agitating shaft
Figure 13 vertical section of a separating device
Figure 14 schematic lateral view of a grinding vessel
Figure 15 part view of a separating device
Figure 16 vertical section of an agitating shaft
35 Figure 17 schematic lateral view of a grinding vessel
Figure 18 vertical section of an agitating shaft
Figure 19 vertical section of an agitating shaft
Figure 20 vertical section of an agitating shaft

5 Figure 21 schematic lateral view of a grinding vessel
Figure 22 vertical section of an agitating shaft
Figure 23 schematic lateral view of a grinding vessel
The agitating ball mill according to the invention consists of a housing 10 in which a
10 drive 12 in form of an electric motor is seated. The drive is in connection with a drive
shaft 16 by means of a drive belt 14. This drive shaft merges with the bearing shaft 18
which in turn is connected with the agitating shaft 20. On the upper side of the bearing
housing 22 is located the grinding stock inlet 24. The grinding chamber 48 is limited by
the grinding vessel 26 surrounding the agitating shaft 20 and the grinding vessel base
15 28. The separating device 30, with which the auxiliary grinding bodies 54 are separated
from the grinding stock, is seated within the agitating shaft 20. To cool or heat the
grinding vessel the latter is surrounded in a double-walled manner by a jacket 32
capable of being cooled and heated. The grinding stock leaves the grinding vessel via a
central grinding stock outlet which leads from the agitating shaft via the bearing shaft as
20 far as the drive shaft. Figure 2 shows the arrangement of a spiral 36 within the agitating
shaft 20 in whose surface agitating bars 38 are inserted. Here, the grinding stock flows
out centrally from the grinding vessel 26 via a line 40 which merges into a pipeline 42.
Figure 3 discloses the embodiment of a spiral for example employed for separating the
25 auxiliary grinding bodies from the grinding stock. This spiral 36 in this case extends
over 720°. The grinding stock flowing into the spiral reaches the grinding stock outlet
through the pipeline 40. In order to bring about relief of the separating device the
auxiliary grinding bodies are transported back into the grinding chamber 48 via
passages 46 in the agitating shaft even before entering the screw passageway 44.
30
Exemplary embodiments of the arrangement of the spiral can be seen in Figures 4 and 5
where the spirals 36 each extend about 360°. In Figure 4 the spiral consists of bars, in
Figure 6 of triangular profiles. Through these inner surfaces of the spirals that can be
described as rough in the widest sense the effect of retention by friction which occurs
35 during the stationary state of the agitating shaft is supported. To increase this retention-
by-friction effect the embodiment of the spiral in Figures 4 and 6 can be increased by
extending the spiral.

5 Figure 5 explains the embodiment of the passages 46 whose lateral surfaces 50 are
directed tangentially to the centre axis of the agitating shaft. Figure 7 shows a separating
device 30 which comprises one or several spirals 36. Depending on how long the
distance of the individual auxiliary grinding bodies in the spiral is, the fewer revolutions
will the separate drive 52 have to complete in order to bring about entering of the
10 auxiliary grinding bodies in the grinding stock outlet.
In Figure 8 the separating device 30 is likewise rotated with a drive 52 separated from
the agitating shaft 20. In addition, the separating device 30 in this case is located in a
hollow space within the agitating shaft 20 as a result of which it is substantially
15 protected against excessive wear through the auxiliary grinding bodies 54 activated by
the agitating shaft 20. Purely schematically it is also shown in this exemplary
embodiment how the auxiliary grinding body concentration decreases from the grinding
chamber 48 in the direction of the grinding stock outlet 34.
20 In Figures 9 and 10 it can be seen that the separating device operates with a right-hand
rotating as well as a left-hand rotating spiral. In the final analysis it is not critical that
the spiral rotates in the direction of rotation opposite to that of the agitating shaft. The
function of the spiral is independent of the direction of rotation of the agitating shaft.
25 In the case of the agitating ball mill shown in Figure 11 the separating device 30 rotates
synchronously with the agitating shaft 20. The spiral 36 of the separating device rests
against the agitating shaft with its left side and with the right side is clamped to the
agitating shaft with a clamping element 56. Centrally in the longitudinal centre of the
spiral in the region of the longitudinal axis of the agitating shaft 20 is located the inlet
30 58 of the grinding stock outlet 34. Figure 12 illustrates in this case the length of the
spiral 36 which in this case comprises a range of 630°.
The embodiment of the separating device according to Figures 13, 14 and 15 is more
preferably geared up for high-viscosity substances. Since the adhesion forces between
35 the product and the auxiliary grinding bodies are very great in high-viscosity
substances, a longer distance for separating the auxiliary grinding bodies is required,
which is why two spirals 36 are provided in Figure 13. Here, the outer surfaces of the
spirals each act like deflectors as far as the start of the further screw. This means that

these surfaces 60 generate a pulsating effect in the direction of the grinding chamber
and thus bring about a deflection of the auxiliary grinding bodies in the direction of the
grinding chamber even at the circumference of the separating device. In addition to
this, the auxiliary grinding bodies during the course of the spiral passageways which
extend over 1080° are continuously forced to return into the grinding chamber through
the friction forces on the spiral walls and the inverse conveying direction.
The Figure 14 shows the use of the spirals 36 described in Figure 13. The separating
device here is directly located on the end face of the cantilever-mounted agitating shaft
20. The product flows out centrally via the agitating shaft 20 and bearing shaft 18.
In Figure 15 the grinding vessel base 28 comprises a shoulder 60. In this region the
spiral 36 is open in the direction of the shoulder so thai: the auxiliary grinding bodies can
flow back into the grinding chamber 48 via short distances. The outer region of the
spiral 36 is limited by a ring 62.
Figures 16 and 17 show separating devices with two spirals each of which extends over
a range of 500° and 560°. The two spirals have screw passageways with always constant
wall distance A. The separating device 30 rotates jointly with the agitating shaft 20,
wherein the product outlet is effected through the agitating shaft 20 and bearing shaft
18. To avoid dead zones in which no grinding stock grinding body flow is generated, a
shoulder 60 is embodied in the separating device which is used for flow formation. The
agitating shaft in this exemplary embodiment comprises no grinding pins 31 but cleats
62.
Figures 18, 19, 20 and 21 demonstrate the position and the embodiment of separating
devices with spirals whose distance is embodied constant as in Figure 18, reducing as in
Figure 19 and expanding as in Figure 20. Figure 18 here corresponds to Figure 16 where
the distance A remains constant over the entire arrangement of the two spirals 36. In
Figure 19 the spirals 36 are arranged so that the distance B from the grinding chamber
to the outlet is reduced. This version is particularly used when low-viscosity material is
employed and it must be expected that the agitating ball mill will be briefly put out of
operation. Through the reducing distance between the two spirals the retention-by-
friction effect between the spiral walls and the auxiliary grinding bodies is reinforced.

Through the arrangement of the two spirals according to Figure 20 it is possible to
achieve a faster outflow of the product following the separation from the auxiliary
grinding bodies. The shown geometry of the two spirals 36 shows that the distance C
increases in the direction from the grinding chamber to the grinding stock outlet.
A further possibility of transporting auxiliary grinding bodies from the region of the
separating device laterally from the spiral passageways back into the grinding chamber
is shown in Figure 23. Here the separating device 30 is seated within a hollow space 64
which is open on one side within the agitating shaft. The spiral 36 is held by the
agitating shaft 20. At the face end of the spiral 36 facing the grinding vessel base 28 is
located a ring 66 which connects each spiral passageway with the hollow space 64 thus
offering the grinding auxiliary bodies the possibility of flowing from the spiral via the
hollow space back into the grinding chamber 48. The ring has a slot 68 through which
the auxiliary grinding bodies can flow back into the grinding chamber via the hollow
space 64. The processed grinding stock leaves the grinding chamber from the central
region within the spiral/s 36 via an immersion pipe 70. As is evident from Figure 22 this
separating device comprises only one spiral 36.

List of reference number
10 Housing
12 Drive
14 Drive belt
16 Drive shaft
18 Bearing shaft
20 Agitating shaft
22 Bearing housing
24 Grinding stock inlet
26 Grinding vessel
28 Grinding vessel base
30 Separating device
32 Jacket
34 Grinding stock outlet
36 Spiral
38 Agitating bars
40 Line
42 Pipe line
44 Spiral passageway
46 Passages
48 Grinding chamber
50 Surfaces
52 Drive
54 Auxiliary grinding body
56 Clamping element
58 Inlet
60 Displacement body
62 Cleat
64 Hollow space
66 Ring
68 Slot
70 Immersion pipe

Patent claims
1.
An agitating ball mill with a cylindrical grinding vessel (26) comprising at least one
grinding stock inlet (24) and at least one grinding stock outlet (34) wherein in the
grinding vessel (26) an agitating shaft (20) connected with a drive (12) is arranged
which transmits a part of the drive energy to auxiliary grinding bodies (54) which are
loosely arranged in the grinding vessel (26) and a separating device (30) arranged in
front of the grinding stock outlet (34),
characterized in that
the separating device (30) consists of at least one spiral (36).
2.
The agitating ball mill according to Claim 1,
characterized in that
the separating device (30) consists of two spirals (36).
3.
The agitating ball mill according to Claim 1,
characterized in that
the spirals (36) are arranged with a constant distance to each other.
4.
The agitating ball mill according to Claim 1,
characterized in that
the spirals (36) are arranged with a varying distance to each other.

5.
The agitating ball mill according to Claim 1,
characterized in that
the radial inner end of the spiral/s (36) ends directly at the grinding stock outlet (34).
6.
The agitating ball mill according to Claim 1,
characterized in that
the grinding stock outlet (34) extends on both sides from the longitudinal centre of the
spiral/s (36).
7.
The agitating ball mill according to Claim 1,
characterized in that
the spiral/s (36) extend/s about a circumference of at least 180°.
8.
The agitating ball mill according to Claim 7,
characterized in that
the spirals (36) extend about a circumference of at least 360°.
9.
The agitating ball mill according to Claim 1,
characterized in that
the width of the spiral/s (36) amounts to at least 1/3 of its diameter.

10.
The agitating ball mill according to Claim 1,
characterized in that
the spiral/s (36) is/are rotated by a drive (52) independent of the agitating shaft (20).
11.
The agitating ball mill according to any one of the Claims 1 to 10,
characterized in that
the separating device (30) consisting of at least one spiral (36) is arranged between the
agitating shaft surface and the longitudinal axis of the agitating shaft (20).
12.
The agitating ball mill according to Claim 11,
characterized in that
the agitating shaft (20) in the region of the spiral/s (36) is embodied hollow and has
openings.
13.
The agitating ball mill according to Claim 12,
characterized in that
the passages (46) are embodied as parallel slots whose inclination is contrary to the
direction of rotation of the agitating shaft (20).
14.
The agitating ball mill according to Claim 13,
characterized in that
the passages (46) in the agitating shaft (20) are oriented tangentially or asymmetrically
to the longitudinal axis of said agitating shaft.

15.
The agitating ball mill according to Claim 11,
characterized in that
the agitating shaft (20) in the region of the spiral/s (36) comprises agitating bars (38).
16.
The agitating ball mill according to Claim 15,
characterized in that
the agitating bars (38) or cleats (62) are offset relative to one another by at least 45°.
17.
The agitating ball mill according to Claim 11,
characterized in that
the spiral/s (36) is/are connected with the agitating shaft (20).
18.
The agitating ball mill according to Claim 1,
characterized in that
the grinding stock outlet (34) is realised through the agitating shaft (20).
19.
The agitating ball mill according to Claim 1,
characterized in that
the grinding stock outlet (34) is realised through a static immersion pipe (70) arranged
in the centre of the spiral (36).

20.
The agitating ball mill according to any one of the preceding claims,
characterized in that
the spiral/s (36) consist/s of individual bars spaced from one another.
21.
The agitating ball mill according to any one of the preceding claims,
characterized in that
the diameter of the spirals (36) amounts to at least 30% of the grinding chamber
diameter.
22.
The agitating ball mill according to any one of the preceding claims,
characterized in that
the diameter of the spiral/s (36) amounts to at least 30% of the diameter of the hollow
space in the agitating ball mill.
23.
The agitating ball mill according to any one of the preceding claims,
characterized in that
the spiral/s (36) is/are inserted laterally between two holohedral end faces.
24.
The agitating ball mill according to any one of the preceding claims,
characterized in that
the spiral/s (36) comprise/s end face/s provided with openings on one or both sides.
25.
The agitating ball mill according to any one of the preceding claims,

characterized in that
a displacement body (60) laterally engages in the spiral/s (36).
26.
The agitating ball mill according to any one of the preceding claims,
characterized in that
the grinding vessel (26) is arranged horizontally.
27.
The agitating ball mill according to any one of the preceding claims,
characterized in that
at least one lateral bracket on the spiral (36) is provided with slots (38) at one or several
points at a radial distance to the grinding stock outlet (34).
28.
The agitating ball mill according to any one of the preceding claims,
characterized in that
at least one of the inner or outer surfaces of the spiral/s (36) comprises a structured
surface structure.
29.
The agitating ball mill according to Claim 1,
characterized in that
the radially outer ends of several spirals (36) are offset relative to one another by at least
90° each.

Agitating ball mill with a cylindrical grinding vessel (26) comprising at least one
grinding stock inlet (24) and at least one grinding stock outlet (34) wherein in the
grinding vessel (26) an agitating shaft (20) connected with a drive (12) is arranged
which transmits a part of the drive energy to auxiliary grinding bodies (54) which are
loosely arranged in the grinding vessel (26) and a separating device (30) arranged in
front of the grinding vessel outlet (34).

Documents:

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Patent Number 272025
Indian Patent Application Number 1501/KOL/2008
PG Journal Number 12/2016
Publication Date 18-Mar-2016
Grant Date 14-Mar-2016
Date of Filing 01-Sep-2008
Name of Patentee NETZSCH-FEINMAHLTECHNIK GMBH
Applicant Address SEDANSTRASSE 70, D-95100 SELB
Inventors:
# Inventor's Name Inventor's Address
1 HORST PAUSCH MAX-REGER-STR. 3, D-95126 SCHWARZENBACH/SAALE
PCT International Classification Number B02C17/00
PCT International Application Number N/A
PCT International Filing date
PCT Conventions:
# PCT Application Number Date of Convention Priority Country
1 DE102007043670.1 2007-09-13 Germany