CN205164894U - Processing system of clay thick liquid - Google Patents
Processing system of clay thick liquid Download PDFInfo
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- CN205164894U CN205164894U CN201520855665.0U CN201520855665U CN205164894U CN 205164894 U CN205164894 U CN 205164894U CN 201520855665 U CN201520855665 U CN 201520855665U CN 205164894 U CN205164894 U CN 205164894U
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Abstract
The utility model provides a processing system of clay thick liquid which characterized in that: this system includes ball -milling device, a raw material handling portion and a slurry transferring portion of a title material portion, a raw materials transport portion, plural number, title material portion carries all kinds of raw materialss of inferior officer to convey respectively to each ball -milling device or raw material handling portion through the raw materials, raw materials transport portion is equipped with second transfer chain, a third transfer chain of a first transfer chain, plural number, the ball -milling device of plural number, the one end of each ball -milling device all communicate the second transfer chain of this raw materials transport portion, and the end is then communicate this slurry transferring portion in addition, raw material handling portion, intercommunication third transfer chain and input the clay to via a fourth transfer chain input water liquid, via 1 the 5th a transfer chain input additive, be processed into clay thick liquid with clay, this water liquid and additive again, slurry transferring portion includes the 7th transfer chain of 1 the 6th transfer chain and plural number. The beneficial effects of the utility model are that: have more the grinding efficiency, promote prescription mud the quality, save a large amount of electric power to and reduction equipment loss.
Description
Technical field
The utility model relates to a kind of grinding system, particularly a kind for the treatment of system of clay slurry.
Background technology
Often there is such determination in known grinding system: 1, the quality of mud is more unstable.Clay and pellet directly input in ball mill device and grind by known grinding system, after ball mill device starts, when the abrasive article (such as ballstone) of its inside strikes pellet, pellet can be pulverized, but when striking clay, major part is but directly stick on clay, or it is not impact is absorbed by clay, good to the abrasive action of clay.2, a large amount of electric power is consumed.Commonly use grinding system system clay, pellet and water are directly inputted in ball mill device to grind, clash into pellet at grinding initial stage abrasive article (such as ballstone), pellet can be broken up, but the abrasive article of plural number clashes into clay, has non-quantitative and is attached on clay.3, equipment loss is increased.Known system because usually completing grinding clay in the given time, and need extend the utilization rate (time) of ball mill device, the overlong time of invalid grinding phase, and equipment cannot effectively do work, and increasing loss, is the shortcoming commonly using device.Therefore, be necessary to research and develop new structure to solve above-mentioned shortcoming.
Utility model content
The purpose of this utility model is the treatment system providing a kind of clay to starch, in order to solve above-mentioned existing issue.
The technical solution of the utility model is as follows: a kind for the treatment of system of clay slurry, is characterized in that: this system comprises a weighing portion, a feedstock transportation portion, plural ball mill device, a Feedstock treating portion and a slurry transferring portion; All kinds of raw material is sent to each ball mill device or Feedstock treating portion through feedstock transportation portion by weighing portion respectively; Feedstock transportation portion is provided with the second pipeline, one the 3rd pipeline of one first pipeline, plural number; The ball mill device of plural number, one end of each ball mill device is all communicated with second pipeline in this feedstock transportation portion, and another end is then communicated with this slurry transferring portion; Feedstock treating portion, is communicated with the 3rd pipeline and inputs clay, and inputting a water liquid via one the 4th pipeline, then inputting an additive via one the 5th pipeline, clay, this water liquid and additive is processed into a clay slurry; Slurry transferring portion comprises the 7th pipeline of one the 6th pipeline and plural number.
First pipeline, it is communicated with weighing portion; Second pipeline, its one end is all communicated with the first pipeline, and another end is then communicated with each ball mill device respectively, and transmits a pellet to each ball mill device for weighing portion; 3rd pipeline, is communicated with the first pipeline and this Feedstock treating portion, and for weighing portion, clay is sent to Feedstock treating portion.
6th pipeline is communicated with Feedstock treating portion, and for clay slurry input slurry transferring portion; The 7th its one end of pipeline of plural number is all communicated with the 6th pipeline, and another end is then communicated with each ball mill device respectively, all establishes a valve body before each the 7th pipeline to each ball mill device.
A sieving equipment is provided with, by the clay pulp screen of preliminary working except the foreign material such as branch form the purer clay slurry of quality between 6th pipeline, the 7th pipeline.
Arbitrary ball mill device can the abrasive article of its inside, and pellet and quality more uniform clay slurry co-ground are become a homogeneous formula mud.
Ball mill device is erected on a holder, and ball mill device can also comprise power set further again, and it is provided with a power source, and power source drives a link driving element through an actuated element, then is rotated by link driving element drive ball mill apparatus.
The beneficial effects of the utility model are: have more grinding efficiency, promote the quality of formula mud, save a large amount of electric power, and reduce equipment loss.
Accompanying drawing explanation
Fig. 1 is the block diagram of the utility model process of lapping;
Fig. 2 is the schematic diagram of the utility model grinding system;
Fig. 3 is the application state schematic diagram of the utility model part-structure.
Indicate in figure: 10, weighing portion, 20, feedstock transportation portion, 21, first pipeline, 22, second pipeline, 23, 3rd pipeline, 30, ball mill device, 31, abrasive article, 32, holder, 40, Feedstock treating portion, 401, 4th pipeline, 402, . the 5th pipeline, 41, water liquid, 42, additive, 50, slurry transferring portion, 501, 6th pipeline, 502, 7th pipeline, 51, valve body, 52, sieving equipment, 60, power set, 61, power source, 62, actuated element, 63, link driving element, 71, pellet, 72, clay is starched, 73, formula mud.
Detailed description of the invention
By reference to the accompanying drawings, the utility model is described in further detail.
A kind for the treatment of system of clay slurry, it is characterized in that: this system comprises a feedstock transportation portion 20 of weighing portion 10, plural ball mill device 30, Feedstock treating portion 40 and a slurry transferring portion 50, and all kinds of raw material is sent to each ball mill device 30 or Feedstock treating portion 40 through feedstock transportation portion 20 by weighing portion 10 respectively; Feedstock transportation portion 20 is provided with the second pipeline 22, the 3rd pipeline 23 of one first pipeline 21, plural number; The ball mill device 30 of plural number, one end of each ball mill device 30 is all communicated with second pipeline 22 in this feedstock transportation portion 20, and another end is then communicated with this slurry transferring portion 50; Feedstock treating portion 40, is communicated with the 3rd pipeline 23 and inputs clay, and inputting a water liquid 41 via one the 4th pipeline 401, then inputting an additive 42 via one the 5th pipeline 402, clay, this water liquid 41 and additive 42 is processed into a clay slurry 72; Slurry transferring portion 50 comprises the 7th pipeline 502 of one the 6th pipeline 501 and plural number.: the first pipeline 21, it is communicated with weighing portion 10; Second pipeline 22, its one end is all communicated with the first pipeline 21, and another end is then communicated with each ball mill device 30 respectively, and transmits a pellet 71 to each ball mill device 30 for weighing portion 10; 3rd pipeline 23, is communicated with the first pipeline 21 and this Feedstock treating portion 40, and for weighing portion 10, clay is sent to Feedstock treating portion 40.6th pipeline 501 is communicated with Feedstock treating portion 40, and for clay slurry 72 input slurry transferring portion 50; The 7th its one end of pipeline 502 of plural number is all communicated with the 6th pipeline 501, and another end is then communicated with each ball mill device 30 respectively, all establishes a valve body 51 before each the 7th pipeline 502 to each ball mill device 30.Be provided with a sieving equipment 52 between 6th pipeline 501, the 7th pipeline 502, the clay of preliminary working slurry 72 screened out the foreign material such as branch and form the purer clay slurry 72 of quality.Arbitrary ball mill device 30 can the abrasive article 31 of its inside, pellet 71 and the more uniform clay of quality is starched the formula mud 73 that 72 co-ground become homogeneous.Ball mill device 30 is erected on a holder 32, and ball mill device 30 can also comprise power set 60 further again, it is provided with a power source 61, and power source 61 drives a link driving element 63 through an actuated element 62, then is rotated by link driving element 63 drive ball mill apparatus 30.
Concrete structure of the present utility model as described above.Say in more detail, hardness is less after absorbing water for the raw material of clay class, and compression strength is little, but has higher viscoelasticity.And the preferred process mode of clay class raw material, be give fine grinding again after first disperseing (mode of such as cutting off) to become the clay of block.But, the compression that ball mill device 30 provides, impact and friction processing, and cannot effective dispersed shale at short notice.
Therefore, the utility model is before clay enters ball mill device 30, first with weighing portion 10 through first and the 3rd pipeline 21 and 23, clay is sent to Feedstock treating portion 40, Feedstock treating portion 40 hydrous water liquid 41 and additive 42, with the cutting knife principle of similar cultivator, clay clay preliminary treatment is become to starch 72, send clay slurry 72 to sieving equipment 52 further, the foreign material sieves such as the branch in the clay of preliminary treatment slurry 72 remove by sieving equipment 52, become the clay slurry 72 that quality is comparatively pure.
And from the 7th pipeline 502, comparatively uniform for quality clay slurry 72 is sent in ball mill device 30, to coordinate abrasive article 31 (such as hard sphere body) and pellet 71 fine grinding in the lump of plural number, because clay has been pre-processed into the comparatively uniform clay slurry 72 of quality.
Consult the first figure, in the operation of actual production line, weighing portion 10 is except being communicated with the 3rd pipeline 23 from the first pipeline 21, clay is delivered to outside Feedstock treating portion 40, also can according to setting, by pellet 71 from the first pipeline 21 through arbitrary second pipeline 22, be delivered in arbitrary ball mill device 30 (being such as delivered to the first, the 3rd ball mill device 30).
And coordinate aforementioned input to have the first, the 3rd ball mill device 30 of pellet 71, only open the valve body 51 on the 7th pipeline 502 corresponding thereto, then clay slurry 72 is from the 7th pipeline 502 input the first, the 3rd ball mill device 30, coordinates pellet 71 attrition process.
No matter expand several ball mill device 30, as long as in parallel with 502 with the first, the 7th pipeline 21, pellet 71 can be accepted respectively and starch 72 with clay, and give fine grinding processing.
If clay and pellet 71 are directly inputted ball mill device 30 grind, then because clay has higher viscoelasticity, therefore, at least need the time of about 20 hours just can complete fine grinding processing, do not considering the moon in summer (June is to September), the non-moon in summer (month beyond the moon in summer) and spike or under the prerequisite of peak time, if with the grinding system in past, and at ten two in first day morning to the next morning eight time (20 totally hours) working hour, suppose that two production lines start eight (power consumption be one hour 100 kilowatts) ball mill devices 30 altogether, one time attrition process approximately needs 20 hours (if clay grinding result badly, then need to extend milling time again, also more electricity charge are consumed).
But, after using the utility model grinding system instead, because of arrange Feedstock treating portion 40 in advance clay is processed into clay slurry 72, one start namely effectively grind, a large sum of electricity charge will be saved, virtually also reach the object of economize energy.
Details are as follows for advantage of the present utility model and effect: the quality 1, promoting formula mud.After the clay of one-tenth block is first given mixed water and additive by the utility model, anticipate and screen out branch and other impurity by sieving equipment, become the clay slurry that quality is comparatively pure, and namely a startup grinding effectively grinds, the time and the quality that are ground to required fineness are all very stable, effectively promote the quality of the sinter that subsequent production goes out.2, a large amount of electric power is saved.Clay of the present utility model is before input ball mill device, and first pretreatment becomes clay to starch, and namely one starts grinding effectively grinds, therefore significantly can shorten milling time, saves a large amount of electric power.3, equipment loss is reduced.Clay of the present utility model first becomes clay to starch by Feedstock treating portion hydrous water with additive treating, therefore, when inputting ball mill device and coordinating pellet grinding, do not have abrasive article to be easy to be cemented on clay, thus extend the disappearance of ball mill device working application time, reduce loss and the utilization rate of ball mill device.
Claims (6)
1. a treatment system for clay slurry, is characterized in that:
This system comprises a weighing portion (10), a feedstock transportation portion (20), plural ball mill device (30), a Feedstock treating portion (40) and a slurry transferring portion (50);
All kinds of raw material is sent to each ball mill device (30) or Feedstock treating portion (40) through feedstock transportation portion (20) by weighing portion (10) respectively;
Feedstock transportation portion (20) is provided with the second pipeline (22), one the 3rd pipeline (23) of one first pipeline (21), plural number;
The ball mill device (30) of plural number, one end of each ball mill device (30) is all communicated with second pipeline (22) in this feedstock transportation portion (20), and another end is then communicated with this slurry transferring portion (50);
Feedstock treating portion (40), be communicated with the 3rd pipeline (23) and input clay, and input a water liquid (41) via one the 4th pipeline (401), input an additive (42) via one the 5th pipeline (402) again, clay, water liquid (41) and additive (42) are processed into clay slurry (72);
Slurry transferring portion (50) comprises the 7th pipeline (502) of one the 6th pipeline (501) and plural number.
2. the treatment system of a kind of clay slurry according to claim 1, it is characterized in that: the first pipeline (21), it is communicated with weighing portion (10); Second pipeline (22), its one end is all communicated with the first pipeline (21), and another end is then communicated with each ball mill device (30) respectively, and transmits a pellet (71) to each ball mill device (30) for weighing portion (10); 3rd pipeline (23), is communicated with the first pipeline (21) and this Feedstock treating portion (40), and clay is sent to Feedstock treating portion (40) for weighing portion (10).
3. the treatment system of a kind of clay slurry according to claim 1, is characterized in that: the 6th pipeline (501) is communicated with Feedstock treating portion (40), and for clay slurry (72) input slurry transferring portion (50); The 7th pipeline (502) its one end of plural number is all communicated with the 6th pipeline (501), and another end is then communicated with each ball mill device (30) respectively, and each the 7th pipeline (502) all establishes a valve body (51) to each ball mill device (30) is front.
4. the treatment system of a kind of clay slurry according to claim 3, it is characterized in that: between the 6th pipeline (501), the 7th pipeline (502), be provided with a sieving equipment (52), the clay of preliminary working is starched (72) screen out the foreign material such as branch form quality purer clay slurry (72).
5. the treatment system of a kind of clay slurry according to claim 1, it is characterized in that: arbitrary ball mill device (30) can the abrasive article (31) of its inside, and pellet (71) and quality more uniform clay slurry (72) co-ground are become homogeneous formula mud (73).
6. the treatment system of a kind of clay slurry according to claim 1, it is characterized in that: ball mill device (30) is erected on a holder (32), and ball mill device (30) can also comprise power set (60) further again, it is provided with a power source (61), power source (61) drives a link driving element (63) through an actuated element (62), then is rotated by link driving element (63) drive ball mill apparatus (30).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520855665.0U CN205164894U (en) | 2015-11-01 | 2015-11-01 | Processing system of clay thick liquid |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520855665.0U CN205164894U (en) | 2015-11-01 | 2015-11-01 | Processing system of clay thick liquid |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205164894U true CN205164894U (en) | 2016-04-20 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201520855665.0U Withdrawn - After Issue CN205164894U (en) | 2015-11-01 | 2015-11-01 | Processing system of clay thick liquid |
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| CN (1) | CN205164894U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105233951A (en) * | 2015-11-01 | 2016-01-13 | 宁波平海建材有限公司 | Treatment system for clay paste |
-
2015
- 2015-11-01 CN CN201520855665.0U patent/CN205164894U/en not_active Withdrawn - After Issue
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105233951A (en) * | 2015-11-01 | 2016-01-13 | 宁波平海建材有限公司 | Treatment system for clay paste |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| AV01 | Patent right actively abandoned |
Granted publication date: 20160420 Effective date of abandoning: 20170714 |
|
| AV01 | Patent right actively abandoned |