CN209254878U - A kind of wet process italic continuous type ball mill - Google Patents
A kind of wet process italic continuous type ball mill Download PDFInfo
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- CN209254878U CN209254878U CN201821622154.4U CN201821622154U CN209254878U CN 209254878 U CN209254878 U CN 209254878U CN 201821622154 U CN201821622154 U CN 201821622154U CN 209254878 U CN209254878 U CN 209254878U
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Abstract
This application discloses a kind of wet process italic continuous type ball mills, the ball mill includes at least three-level ball milling unit, feed inlet, motor, bracket and grout outlet, the first order ball milling unit is fixedly connected with the second level ball milling unit, the second level ball milling unit is fixedly connected with the third level ball milling unit, the diameter of the first order ball milling unit is greater than the diameter of the second level ball milling unit, and the diameter of the second level ball milling unit is greater than the diameter of the third level ball milling unit；The three-level ball milling unit is placed by least four riding, and the motor and feed inlet are respectively arranged on the first order ball milling unit at top, and the bottom of the three-level ball milling unit is arranged in the grout outlet.The ball mill slant setting reduces occupied space, and charging is continuous with pulp, saves the time.
Description
Technical field
The utility model relates to milling machinery field more particularly to a kind of wet process italic continuous type ball mills.
Background technique
Currently, ball mill is the key equipment that material is broken and then is crushed, it is widely used in Production of Ceramics row
Industry.
However, the shortcomings that traditional wet intermittent ball grinder is that there are following main problems:
1. grinding efficiency is low, in wet intermittent ball grinder, there are a large amount of materials effectively not crushed and be mingled with
In the material crushed, causes material to be difficult to quickly be ground, reduce efficiency；
2. energy consumption is high, the cylinder of wet intermittent ball grinder greatly and again, the drive of motor quickly rotate need to expend it is huge
Big electric power energy；
3. the ball milling period is long, when degree of grinding of the raw material in intermittent ball mill will reach requirement and need to spend a large amount of
Between；
4. charging and blowing are discontinuous, wet intermittent ball grinder charging or blowing are both needed to pause the operation of a machine, so that
Charging and blowing can not obtain continuity；
5. complete machine occupied space is big, the machine volume of wet intermittent ball grinder is big and the mode of traverse is used to make complete machine
Required the space occupied is required big.
Therefore, how to solve the problems, such as said one or several, become urgent problem to be solved.
Utility model content
In order to solve deficiency in the prior art, the application provides a kind of wet process italic continuous type ball mill.
This application discloses a kind of wet process italic continuous type ball mill, the ball mill include at least three-level ball milling unit,
Feed inlet, motor, bracket and grout outlet, the three-level ball milling unit include first order ball milling unit, second level ball milling list
Member and third level ball milling unit；Wherein,
The first order ball milling unit is fixedly connected with the second level ball milling unit, the second level ball milling unit and institute
It states third level ball milling unit to be fixedly connected, the diameter of the first order ball milling unit is greater than the straight of the second level ball milling unit
Diameter, the diameter of the second level ball milling unit are greater than the diameter of the third level ball milling unit；
The three-level ball milling unit is placed by least four riding, and the motor and feed inlet are respectively arranged at position
In on the first order ball milling unit at top, the bottom of the three-level ball milling unit is arranged in the grout outlet.
In one possible implementation, the first order ball milling unit includes the first ball milling chamber, the first abrasive media
Body, the first track and first order sieve；The second level ball milling unit includes the second ball milling chamber, the second grinding medium plastid, second
Track and second level sieve；The third level ball milling unit include third ball milling chamber, third grinding medium plastid, third track with
And third level sieve.
In one possible implementation, the filtering bore dia of the first order sieve is greater than the second level sieve
Filter bore dia；The filtering bore dia of the second level sieve is greater than the filtering bore dia of the third level sieve.
In one possible implementation, the diameter of first track is greater than the diameter of second track；It is described
The diameter of second track is greater than the diameter of the third track.
In one possible implementation, the diameter of the first grinding medium plastid is greater than the second grinding medium plastid
Diameter；The diameter of the second grinding medium plastid is greater than the diameter of the third grinding medium plastid.
In one possible implementation, the volume of the first ball milling chamber is greater than the volume of the second ball milling chamber；
The volume of the second ball milling chamber is greater than the volume of the third ball milling chamber.
The utility model is a kind of wet process italic continuous type ball mill, and the crushing material suitable for ceramic production industry is led
Domain.Wet process italic continuous type ball mill completes slant setting state under the support of bracket 15, and motor 16 is then ball mill
Quickly rotation provides enough power.Enter wet process italic continuous type ball mill from feed inlet 1 by broken material
Ball milling chamber 2 has track 14 and grinding medium plastid 3 in ball milling chamber 2, and wherein grinding medium plastid 3 is the pottery with high rigidity
Sphere made of ceramic material.The quick rotation that grinding medium plastid 3 is followed by ball mill enters tilting high speed circular along track 14
All motion states, into the material after ball milling chamber 2 in a section track by the grinding medium plastid 3 of high-speed motion repeatedly
It rolls, hit, complete first time pulverization process, smashed material enters next ball milling chamber 4 by level-one sieve 13 for the first time
Second of pulverization process of middle progress.
Into ball milling chamber 4 material by the high-speed motion in track 12 the rolling repeatedly of grinding medium plastid 5, hit and
Generate second of pulverization process.
Second smashed material is entered in ball milling chamber 6 by second level sieve 11, into ball milling chamber 6 material by rail
The grinding medium plastid 7 of high-speed motion in road 10 rolls repeatedly, hits and generate third time pulverization process, after third time crushes
Material flowed out from grout outlet 8 after the filtering of three-level sieve 9.Revolving speed by calculating ball mill adjusts the fortune of motor 16
The size of row power obtains the material of required degree of grinding to reach；Charging can be carried out continuously with pulp, be handled without shutdown；
The quality of crushing material is ensured with screening three times by grinding three times.
The structure design of the utility model is reasonable, compact layout, and various function parts are coordinated uniformly, organically to form one
Whole, reliable performance is continuously automatically performed the charging, crushing and pulp of material, good crushing effect, the control of crushing material process
It is very easy.Wet process italic continuous type ball mill has the advantage that compared with wet intermittent ball grinder
1. grinding efficiency is high, pass through the screening of the sieve of the grinding and three levels of three levels, the machine of serialization
Operation, improves the efficiency of grinding；
2. low energy consumption, operated by the production of machinery of serialization, the grinding cavit design of three-level, so that the weight of ball mill
It is reduced, reduces energy consumption；
3. the ball milling period is short, the tilting design of ball mill makes the material being crushed under gravity
The other ball milling chamber of next stage is rapidly entered by sieve, completes quickly to flow out from grout outlet after crushing；
4. feed it is continuous with pulp, material can in the case where wet process italic continuous type ball mill continuous running quickly from into
It is fed at material mouth 1, and can persistently locate slurry by grout outlet 8；
5. complete machine occupies little space, is designed, subtracted by the three-stage of the ball milling cavity to wet process italic continuous type ball mill
The small volume and weight of single hop ball milling chamber, and tilting placement then reduces the space occupied needed for complete machine.This solves wet
Five problems present in method intermittent ball mill.
Detailed description of the invention
It, below will be to required in embodiment description in order to illustrate more clearly of the technical solution of the utility model embodiment
The attached drawing used is briefly described, it should be apparent that, the accompanying drawings in the following description is only some embodiments of utility model,
For those of ordinary skill in the art, without creative efforts, it can also be obtained according to these attached drawings
Other attached drawings.
Fig. 1 is a kind of structural schematic diagram for wet process italic continuous type ball mill that present specification embodiment provides；
Fig. 2 is a kind of ball milling cavity body structure schematic diagram that present specification embodiment provides；
Fig. 3 is another ball milling cavity body structure schematic diagram that present specification embodiment provides；
Fig. 4 is another ball milling cavity body structure schematic diagram that present specification embodiment provides.
Fig. 1-Fig. 4: feed inlet 1, ball milling chamber 2, grinding medium plastid 3, ball milling chamber 4, grinding medium plastid 5, ball milling chamber 6, grinding
Dielectric 7, grout outlet 8, three-level sieve 9, track 10, second level sieve 11, track 12, level-one sieve 13, track 14, bracket 15,
Motor 16.
Specific embodiment
Below by drawings and examples, the technical solution of the utility model is described in further detail.
" first " " second " in the embodiment of the present application is also convenient just for the sake of description, can not be interpreted as to the application
The restriction of specification embodiment.
As shown in Figure 1, a kind of wet process italic continuous type ball mill, the ball mill include at least three-level ball milling unit, into
Material mouth 1, motor 16, bracket 15 and grout outlet 8, the three-level ball milling unit include first order ball milling unit, second level ball
Grind unit and third level ball milling unit；Wherein,
The first order ball milling unit is fixedly connected with the second level ball milling unit, the second level ball milling unit and institute
It states third level ball milling unit to be fixedly connected, the diameter of the first order ball milling unit is greater than the straight of the second level ball milling unit
Diameter, the diameter of the second level ball milling unit are greater than the diameter of the third level ball milling unit；
The three-level ball milling unit is respectively set by 15 slant setting of at least four bracket, the motor 16 and feed inlet 1
In on the first order ball milling unit for being located at top, the bottom of the three-level ball milling unit is arranged in the grout outlet 8.
In one example, the first order ball milling unit includes the first ball milling chamber 2, the first grinding medium plastid 3, the first rail
Road 14 and first order sieve 13；The second level ball milling unit includes the second ball milling chamber 4, the second grinding medium plastid 5, the second track
12 and second level sieve 11；The third level ball milling unit includes third ball milling chamber 6, third grinding medium plastid 7, third track
10 and third level sieve 9.
In one example, the filtering bore dia of the first order sieve 13 is greater than the filter hole of the second level sieve 11
Diameter；The filtering bore dia of the second level sieve 11 is greater than the filtering bore dia of the third level sieve 9.
In one example, the diameter of first track 14 is greater than the diameter of second track 12；Second rail
The diameter in road 12 is greater than the diameter of the third track 10.
In one example, the diameter of the first grinding medium plastid 3 is greater than the diameter of the second grinding medium plastid 5；
The diameter of the second grinding medium plastid 5 is greater than the diameter of the third grinding medium plastid 7.
In one example, the volume of the first ball milling chamber 2 is greater than the volume of the second ball milling chamber 4；
The volume of the second ball milling chamber 4 is greater than the volume of the third ball milling chamber 6.
The utility model is a kind of wet process italic continuous type ball mill, and the crushing material suitable for ceramic production industry is led
Domain.Wet process italic continuous type ball mill completes slant setting state under the support of bracket 15, and motor 16 is then ball mill
Quickly rotation provides enough power.Enter wet process italic continuous type ball mill from feed inlet 1 by broken material
Ball milling chamber 2 has track 14 and grinding medium plastid 3 in ball milling chamber 2, and wherein grinding medium plastid 3 is the pottery with high rigidity
Sphere made of ceramic material.The quick rotation that grinding medium plastid 3 is followed by ball mill enters tilting high speed circular along track 14
All motion states, into the material after ball milling chamber 2 in a section track by the grinding medium plastid 3 of high-speed motion repeatedly
It rolls, hit, complete first time pulverization process, smashed material enters next ball milling chamber 4 by level-one sieve 13 for the first time
Second of pulverization process of middle progress.
Into ball milling chamber 4 material by the high-speed motion in track 12 the rolling repeatedly of grinding medium plastid 5, hit and
Generate second of pulverization process.
Second smashed material is entered in ball milling chamber 6 by second level sieve 11, into ball milling chamber 6 material by rail
The grinding medium plastid 7 of high-speed motion in road 10 rolls repeatedly, hits and generate third time pulverization process, after third time crushes
Material flowed out from grout outlet 8 after the filtering of three-level sieve 9.Revolving speed by calculating ball mill adjusts the fortune of motor 16
The size of row power obtains the material of required degree of grinding to reach；Charging can be carried out continuously with pulp, be handled without shutdown；
The quality of crushing material is ensured with screening three times by grinding three times.
The structure design of the utility model is reasonable, compact layout, and various function parts are coordinated uniformly, organically to form one
Whole, reliable performance is continuously automatically performed the charging, crushing and pulp of material, good crushing effect, the control of crushing material process
It is very easy.Wet process italic continuous type ball mill has the advantage that compared with wet intermittent ball grinder
1. grinding efficiency is high, pass through the screening of the sieve of the grinding and three levels of three levels, the machine of serialization
Operation, improves the efficiency of grinding；
2. low energy consumption, operated by the production of machinery of serialization, the grinding cavit design of three-level, so that the weight of ball mill
It is reduced, reduces energy consumption；
3. the ball milling period is short, the tilting design of ball mill makes the material being crushed under gravity
The other ball milling chamber of next stage is rapidly entered by sieve, completes quickly to flow out from grout outlet after crushing；
4. feed it is continuous with pulp, material can in the case where wet process italic continuous type ball mill continuous running quickly from into
It is fed at material mouth 1, and can persistently locate slurry by grout outlet 8；
5. complete machine occupies little space, is designed, subtracted by the three-stage of the ball milling cavity to wet process italic continuous type ball mill
The small volume and weight of single hop ball milling chamber, and tilting placement then reduces the space occupied needed for complete machine.This solves wet
Five problems present in method intermittent ball mill.
Grinding in 14 medium-high speed sports of track is utilized as shown in Fig. 2, mainly passing through to the material entered in ball milling chamber 2
Grinding media body 3 is carried out first time pulverization process.
It should be noted that grinding medium plastid is sphere made of a kind of ceramic material of high rigidity, in the fast of ball mill
By carrying out high speed circular motion under the collective effect of centrifugal force and inertia force and frictional force in track 14 in fast rotary course,
And then first time pulverization process is carried out to the material entered in ball milling chamber 2.
As shown in figure 3, the volume ratio ball milling chamber 2 of ball milling chamber 4 is slightly smaller, by first time pulverization process from ball milling chamber 2
Material enters ball milling chamber 4 by sieve 13, material on the track 12 the rolling of the grinding medium plastid 5 of high-speed motion, hit
Effect is lower to complete second of pulverization process；More slightly smaller than grinding medium plastid 3 in the volume of grinding medium plastid 5, grinding medium plastid 5 is in ball
By carrying out high speed under the collective effect of centrifugal force and inertia force and frictional force in track 12 in the quick rotary course of grinding machine
Circular motion, and then second of pulverization process is carried out to the material entered in ball milling chamber 4.
As shown in figure 4, the volume of the volume ratio ball milling chamber 4 of ball milling chamber 6 is slightly smaller, crushed from ball milling chamber 4 by second
The material of processing enters ball milling chamber 6, the stone roller of material grinding medium plastid 7 of high speed circular motion on track 10 by sieve 11
Pressure completes second of pulverization process under the action of hitting；, grinding medium more slightly smaller than grinding medium plastid 5 in the volume of grinding medium plastid 7
Plastid 7 in the quick rotary course of ball mill by under the collective effect of centrifugal force and inertia force and frictional force in track 10
High speed circular motion is carried out, and then third time pulverization process is carried out to the material entered in ball milling chamber 6；Third time is completed in material
By being flowed out under the filtering of three-level sieve 9 from grout outlet 8 out of ball milling chamber 6 after pulverization process.
Track 10, as shown in figure 4, effect is that the condition for completing high speed circular motion is provided for grinding medium plastid 7, Yi Jiwei
Grinding medium plastid 7 carries out third time pulverization process to material and provides space；Mistake of the filter hole of second level sieve 11 than three-level sieve 9
Filter opening is slightly larger, enters in ball milling chamber 6 under the filtering of second level sieve 11 by second of smashed material.
Track 12, as shown in figure 3, the internal diameter of track 12 is more slightly larger than the internal diameter of track 10, the effect of track 12 is for grinding
Dielectric 5 provides the condition for completing high speed circular motion, and carries out second of pulverization process to material for grinding medium plastid 5 and mention
For space；The filter hole of level-one sieve 13 is more slightly larger than the filter hole of second level sieve 11, by smashed material for the first time one
Enter in ball milling chamber 4 under the filtering of grade sieve 13.
Track 14, as shown in Fig. 2, the internal diameter of track 14 is more slightly larger than the internal diameter of track 12, the effect of track 14 is for grinding
Dielectric 3 provides the condition for completing high speed circular motion, and carries out first time pulverization process to material for grinding medium plastid 3 and mention
For space.
Bracket 15 shares four angles that four brackets 15 are respectively at wet process italic continuous type ball mill, rises to ball mill
Supporting role；16 motor, effect are to provide enough power for the continuous quick rotation of wet process italic continuous type ball mill.
The working principle of the utility model wet process italic continuous type ball mill is as shown in Figure 1, wet process italic continous way ball
Grinding machine completes heeling condition under the support of bracket 15, and motor 16 then provides enough power for the quick rotation of ball mill.
Material enters that ball milling is intracavitary by feed inlet 1, the grinding medium plastid in track in the quick rotary course of ball mill, by
Centrifugal force, gravity machine frictional force collective effect under carry out high speed circular motion, since the volume of each ball milling chamber is not of uniform size,
The movement velocity of grinding medium plastid between each ball milling chamber is also different, also different to the degree of grinding of material and then right
Material carries out different degrees of pulverization process three times, and there is hole sieves in different size to carry out to material between each chamber
Different degrees of filtering, reach crush require material will after the filtering of three-level sieve 9 from grout outlet 8 flow out.
Wet process italic continuous type ball mill its mainly by first segment ball milling cavity system, second segment ball milling cavity system and third section ball milling chamber
System three parts composition.
1. first segment ball milling cavity system, as shown in Figure 1 and Figure 2, first segment ball milling cavity system includes ball milling chamber 2, abrasive media
Body 3, level-one sieve 13 and 14 4 part of track form.It is continuous to enter wet process italic from feed inlet 1 by broken material
The ball milling chamber 2 of formula ball mill, the quick rotation that the grinding medium plastid 3 in ball milling chamber 2 is followed by ball mill enter along track 14
Tilting high speed circumference motion state, into the material after ball milling chamber 2 by the grinding of high-speed motion in a section track
The rolling, hitting repeatedly of dielectric 3, completes first time pulverization process, and smashed material is entered next by level-one sieve 13
Second of pulverization process is carried out in ball milling chamber 4.
2. second segment ball milling cavity system, as shown in Figure 1, Figure 3, second segment ball milling cavity system includes ball milling chamber 4, abrasive media
Body 5, second level sieve 11 and 12 4 part of track form.Material after first time pulverization process enters from level-one sieve 13
The ball milling chamber 4 of wet process italic continuous type ball mill, the grinding medium plastid 5 in ball milling chamber 4 are followed by the quick rotation edge of ball mill
Track 12 enter tilting high speed circumference motion state, into the material after ball milling chamber 4 by height in a section track
The rolling, hitting repeatedly of grinding medium plastid 5 of speed movement, completes second of pulverization process, and second of smashed material passes through
Second level sieve 11, which enters, carries out third time pulverization process in next ball milling chamber 6.
3. third section ball milling cavity system, as Figure 1 and Figure 4, third section ball milling cavity system includes ball milling chamber 6, abrasive media
Body 7, three-level sieve 9 and 10 4 part of track form.Material after second of pulverization process enters from second level sieve 11
The ball milling chamber 6 of wet process italic continuous type ball mill, the grinding medium plastid 7 in ball milling chamber 6 are followed by the quick rotation edge of ball mill
Track 10 enter tilting high speed circumference motion state, into the material after ball milling chamber 6 by height in a section track
The rolling, hitting repeatedly of grinding medium plastid 7 of speed movement, completes third time pulverization process, and the smashed material of third time passes through
It is spilt out after the filtering of three-level sieve 9 from grout outlet 8.
It should be noted that being illustrated by taking three-level ball mill as an example in this specification embodiment, it is clear that the application is not
The case where terminating in protection three-level ball mill；It can also be set as other levels according to the actual needs.
Above-described specific embodiment, to the purpose of this utility model, technical scheme and beneficial effects carried out into
One step is described in detail, it should be understood that being not used to limit the foregoing is merely specific embodiment of the present utility model
Determine the protection scope of the utility model, within the spirit and principle of the utility model, any modification for being made equally is replaced
It changes, improve, should be included within the scope of protection of this utility model.
Claims (6)
1. a kind of wet process italic continuous type ball mill, which is characterized in that the ball mill includes at least three-level ball milling unit, charging
Mouthful (1), motor (16), bracket (15) and grout outlet (8), the three-level ball milling unit include first order ball milling unit, the
Second level ball milling unit and third level ball milling unit；Wherein,
The first order ball milling unit is fixedly connected with the second level ball milling unit, the second level ball milling unit and described the
Three-level ball milling unit is fixedly connected, and the diameter of the first order ball milling unit is greater than the diameter of the second level ball milling unit, institute
The diameter for stating second level ball milling unit is greater than the diameter of the third level ball milling unit；
The three-level ball milling unit is set respectively by least four bracket (15) slant setting, the motor (16) and feed inlet (1)
It is placed on the first order ball milling unit at top, the bottom of the three-level ball milling unit is arranged in the grout outlet (8).
2. ball mill according to claim 1, which is characterized in that the first order ball milling unit includes the first ball milling chamber
(2), the first grinding medium plastid (3), the first track (14) and first order sieve (13)；
The second level ball milling unit includes the second ball milling chamber (4), the second grinding medium plastid (5), the second track (12) and the
Second level sieve (11)；
The third level ball milling unit includes third ball milling chamber (6), third grinding medium plastid (7), third track (10) and
Three-level sieve (9).
3. ball mill according to claim 2, which is characterized in that the filtering bore dia of the first order sieve (13) is greater than
The filtering bore dia of the second level sieve (11)；
The filtering bore dia of the second level sieve (11) is greater than the filtering bore dia of the third level sieve (9).
4. ball mill according to claim 2, which is characterized in that the diameter of first track (14) is greater than described second
The diameter of track (12)；
The diameter of second track (12) is greater than the diameter of the third track (10).
5. ball mill according to claim 2, which is characterized in that the diameter of the first grinding medium plastid (3) is greater than institute
State the diameter of the second grinding medium plastid (5)；
The diameter of the second grinding medium plastid (5) is greater than the diameter of the third grinding medium plastid (7).
6. ball mill according to claim 2, which is characterized in that the volume of the first ball milling chamber (2) is greater than described the
The volume of two ball milling chambers (4)；
The volume of the second ball milling chamber (4) is greater than the volume of the third ball milling chamber (6).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201821622154.4U CN209254878U (en) | 2018-10-08 | 2018-10-08 | A kind of wet process italic continuous type ball mill |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201821622154.4U CN209254878U (en) | 2018-10-08 | 2018-10-08 | A kind of wet process italic continuous type ball mill |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN209254878U true CN209254878U (en) | 2019-08-16 |
Family
ID=67553533
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201821622154.4U Expired - Fee Related CN209254878U (en) | 2018-10-08 | 2018-10-08 | A kind of wet process italic continuous type ball mill |
Country Status (1)
| Country | Link |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113941404A (en) * | 2020-07-17 | 2022-01-18 | 湖南磊鑫新材料科技有限公司 | Calcium carbonate crushing and grinding device |
| CN114471845A (en) * | 2022-02-15 | 2022-05-13 | 福建长泰万泰矿物制品有限公司 | Silica grinding method |
-
2018
- 2018-10-08 CN CN201821622154.4U patent/CN209254878U/en not_active Expired - Fee Related
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113941404A (en) * | 2020-07-17 | 2022-01-18 | 湖南磊鑫新材料科技有限公司 | Calcium carbonate crushing and grinding device |
| CN113941404B (en) * | 2020-07-17 | 2023-02-28 | 湖南磊鑫新材料科技有限公司 | Calcium carbonate crushing and grinding device |
| CN114471845A (en) * | 2022-02-15 | 2022-05-13 | 福建长泰万泰矿物制品有限公司 | Silica grinding method |
| CN114471845B (en) * | 2022-02-15 | 2023-02-10 | 福建长泰万泰矿物制品有限公司 | Silica grinding method |
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Granted publication date: 20190816 Termination date: 20201008 |