CN203558979U - Standardized continuous treatment production line for ceramic raw materials - Google Patents
Standardized continuous treatment production line for ceramic raw materials Download PDFInfo
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- CN203558979U CN203558979U CN201320789685.3U CN201320789685U CN203558979U CN 203558979 U CN203558979 U CN 203558979U CN 201320789685 U CN201320789685 U CN 201320789685U CN 203558979 U CN203558979 U CN 203558979U
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- 239000002994 raw material Substances 0.000 title claims abstract description 24
- 239000000919 ceramic Substances 0.000 title claims abstract description 18
- 238000004519 manufacturing process Methods 0.000 title abstract description 8
- 238000000498 ball milling Methods 0.000 claims abstract description 42
- 239000002002 slurry Substances 0.000 claims abstract description 29
- 238000001694 spray drying Methods 0.000 claims abstract description 10
- 238000010924 continuous production Methods 0.000 claims description 10
- 238000006243 chemical reaction Methods 0.000 claims description 5
- 239000000843 powder Substances 0.000 abstract description 7
- 238000005265 energy consumption Methods 0.000 abstract description 4
- 239000000203 mixture Substances 0.000 abstract description 3
- 238000007599 discharging Methods 0.000 abstract 1
- 238000000034 method Methods 0.000 description 12
- 238000000227 grinding Methods 0.000 description 4
- 239000011449 brick Substances 0.000 description 3
- 239000002245 particle Substances 0.000 description 3
- 238000001035 drying Methods 0.000 description 2
- 238000001914 filtration Methods 0.000 description 2
- 238000010409 ironing Methods 0.000 description 2
- 239000006148 magnetic separator Substances 0.000 description 2
- 238000003801 milling Methods 0.000 description 2
- 238000000465 moulding Methods 0.000 description 2
- 238000003825 pressing Methods 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000004134 energy conservation Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000005469 granulation Methods 0.000 description 1
- 230000003179 granulation Effects 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 239000011268 mixed slurry Substances 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 239000004576 sand Substances 0.000 description 1
- 239000007921 spray Substances 0.000 description 1
- 239000002351 wastewater Substances 0.000 description 1
- 230000002087 whitening effect Effects 0.000 description 1
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Abstract
The utility model provides a standardized continuous treatment production line for ceramic raw materials. The standardized continuous treatment production line comprises a gravel feeding unit, vertical mill roughing equipment, a continuous ball milling unit, mud-to-slurry equipment, a deironing slurry pool, a plurality of ball milling machines and a spray drying tower, a plurality of gravel feeding machines form the gravel feeding unit which is connected with the vertical mill roughing equipment, the vertical mill roughing equipment is connected with the continuous ball milling unit through a conveying belt, the continuous ball milling unit is formed by connecting the ball milling machines and connected with the deironing slurry pool, a discharging port of the deironing slurry pool is connected with a big slurry pool, a plurality of raw ore mud feeding machines are parallelly connected to form a raw ore mud feeding unit which is connected with the mud-to-slurry equipment, the mud-to-slurry equipment is connected a feeding port of the big slurry pool which is connected with the ball milling machines, the ball milling machines are connected with the spray drying tower. The standardized continuous treatment production line is high in ball milling efficiency, low in energy consumption, stable in powder composition, high in whiteness and low in cost.
Description
Technical field
The utility model relates to the technical field of the manufacturing and processing equipment of ceramic industry, refers in particular to the continuous process for producing line of a kind of ceramic raw material stdn.
Background technology
During ceramic wall and floor bricks is produced at present, Raw material processing treatment process is all to adopt traditional wet type milling method, adopt ball mill to add a certain amount of water to grind to form the mud slurry of water ratio 32%-38% left and right ceramic raw material, then by spray-drying tower slurry drying granulation, slurry drying is become to the moisture of 7% left and right, make and be applicable to the powder that automatic brick pressing machine moulding is used.This traditional wet type milling method Ball-milling Time is long, and grinding efficiency is low, especially for the many polished tile of raw material type, produces applicable intermittent type ball milling, and same ball mill ball milling raw material type is many, rotating wash bowl grinding machine waste water resource and manpower while frequently changing raw material.Although answer energy-conservation situation required, ball mill is carried out to a series of reducing energy consumption measures such as Frequency Conversion Modification, power savings is extremely limited.Had in recent years the dry method powder process that begins one's study of part Ceramics Enterprises, but dry method powder process except the requirement height to raw material moisture, maximum problem is still homogenizing and stability, weakness is that the kind of batching can not be too many.Based on these problem places, how to improve the utilising efficiency of ball mill, shorten Ball-milling Time, increase the stability of raw material, realize stdn and process and seem extremely important and crucial continuously.
Utility model content
The purpose of this utility model is to provide that a kind of grinding efficiency is high, and energy consumption is low, powder stable components, and whiteness is high, the continuous process for producing line of a kind of ceramic raw material stdn that cost is low.
The technique means that the utility model adopts is as follows.The continuous process for producing line of ceramic raw material stdn, it comprises sandstone feeding unit, Vertical Mill roughing equipment, continuous ball milling unit, mudization slurry equipment, deironing stock tank, ball mill and spray-drying tower; Wherein, some sandstone feeding machines form sandstone feeding unit, this sandstone feeding unit connects the opening for feed of Vertical Mill roughing equipment, and the discharge port of this Vertical Mill roughing equipment is connected with the opening for feed of continuous ball milling unit by conveying belt, and this continuous ball milling unit is formed by connecting by some ball mills; The discharge port of this continuous ball milling unit connects the opening for feed of deironing stock tank; The discharge port of deironing stock tank connects the opening for feed of large stock tank; And some raw ore mud feeding machines compose in parallel raw ore mud feeding unit, this raw ore mud feeding unit connects the opening for feed of mud pulp equipment, and the discharge port of mud pulp equipment connects another opening for feed of large stock tank; The discharge port of large stock tank connects ball mill, and ball mill is connected with spray-drying tower.
These some sandstone feeding machines, for being arranged in parallel, form sandstone feeding unit.
This sandstone feeding machine is provided with frequency conversion equipment, with quantitative load processed.
This continuous ball milling unit is that some ball mills are staged connection.
This ball mill is divided into three grades, and after one-level ball mill ball milling, slurry fineness is less than or equal to 0.4mm; After secondary ball mill ball milling, slurry fineness is less than or equal to 0.2mm; After three grades of ball mill ball millings, slurry fineness is less than or equal to 0.1mm.
The beneficial effects of the utility model are as follows.
1, stdn continuous processing technique is to the type of all kinds of sandstones and raw ore mud and granular size, grating without particular requirement, and the raw material without buying after processing, saves production cost greatly.
2, raw material is carried out to classifying type and utilize sandstone feeding unit and raw ore mud feeding unit, realize stdn continuous processing technique stage by stage, grinding efficiency is high, and energy consumption is low.
3, feeding machine can install frequency conversion equipment additional, quantitative load processed, the powder stable components after processing; High frequency deironing function significantly improves whiteness.
Accompanying drawing explanation
Figure 1 shows that production line block diagram of the present utility model.
Embodiment
Refer to shown in Fig. 1, the continuous process for producing line of a kind of ceramic raw material stdn, it comprises sandstone feeding unit 1, Vertical Mill roughing equipment 2, continuous ball milling unit 4, mudization slurry equipment 8, deironing stock tank 5, ball mill 9 and spray-drying tower 10; Wherein, some sandstone feeding machines 11 are arranged in parallel and form sandstone feeding unit 1, this sandstone feeding machine can be provided with frequency conversion equipment with quantitative load processed, this sandstone feeding unit 1 connects the opening for feed of Vertical Mill roughing equipment 2, the discharge port of this Vertical Mill roughing equipment 2 is connected with the opening for feed of continuous ball milling unit 4 by conveying belt 3, and this continuous ball milling unit 4 is formed by connecting by some ball mills 12; The discharge port of this continuous ball milling unit 4 connects the opening for feed of deironing stock tank 5, is generally provided with high frequency magnetic separator de-ironing in deironing stock tank; The discharge port of deironing stock tank 5 connects the opening for feed of large stock tank 6.
And some raw ore mud feeding machines 13 compose in parallel raw ore mud feeding unit 7, this raw ore mud feeding unit 7 connects the opening for feed of mudization slurry equipment 8, and the discharge port of mudization slurry equipment 8 connects another opening for feed of large stock tank 6.
The discharge port of large stock tank 6 connects ball mill 9, and ball mill 9 is connected with spray-drying tower 10.
Wherein, this continuous ball milling unit 4 connects for some ball mills 12 are staged, after upper level ball mill ball milling, expect that the slurry that fineness is less than or equal to the requirement of next stage ball milling particle diameter enters next stage ball mill, the slurry that is greater than particle diameter requirement will rest in upper level ball mill and continue ball milling, until reach, enter the requirement of next stage ball mill particle diameter.
A kind of ceramic raw material stdn continous treatment process of the present utility model, ceramic raw material is wherein divided into sandstone and the large class of raw ore mud two, the type of wherein each class sandstone and raw ore mud and granular size, grating are without particular requirement, all applicable to above-mentioned production line and present method.In the present embodiment, 5 kinds of dissimilar sandstones are delivered to Vertical Mill roughing equipment by ratio requirement by sandstone feeding unit, by Vertical Mill roughing equipment, raw material coarse breaking to fineness is reached to 1mm and be delivered to continuous ball milling unit after following, after one-level ball mill ball milling, fineness is less than or equal to the slurries filtration of 0.4mm to secondary ball mill ball milling, after secondary ball mill ball milling, fineness is less than or equal to slurries filtration to the three grade ball mill ball milling of 0.2mm, after three grades of continuous staged ball millings, slurry below 0.1mm is delivered to and in deironing stock tank, carries out iron-removal and whitening, here can use high frequency magnetic separator de-ironing to carry out deironing, whiteness is increased to 10 degree left and right.Simultaneously, 3 kinds of dissimilar raw ore muds are also delivered to after the sand removed in mud slurry equipment in raw ore mud and impurity and pretreated sandstone slurry mix and blend in stock tank by feeding unit by ratio requirement, and last mixed slurry is spray dried to and is applicable to the powder that automatic brick pressing machine moulding is used with spray-drying tower after being delivered to and being milled to 0.05mm in ball mill.
In the utility model, related all devices is all existing installations, its mode of connection is also that those skilled in the art can learn, choosing and proportioning of this case Raw, all adopt existing current techique to realize, this case key is each equipment to combine, and to carry out stdn, processes continuously and enhances productivity.
Claims (5)
1. the continuous process for producing line of ceramic raw material stdn, is characterized in that, it comprises sandstone feeding unit, Vertical Mill roughing equipment, continuous ball milling unit, mudization slurry equipment, deironing stock tank, ball mill and spray-drying tower;
Wherein, some sandstone feeding machines form sandstone feeding unit, this sandstone feeding unit connects the opening for feed of Vertical Mill roughing equipment, and the discharge port of this Vertical Mill roughing equipment is connected with the opening for feed of continuous ball milling unit by conveying belt, and this continuous ball milling unit is formed by connecting by some ball mills;
The discharge port of this continuous ball milling unit connects the opening for feed of deironing stock tank;
The discharge port of deironing stock tank connects the opening for feed of large stock tank;
And some raw ore mud feeding machines compose in parallel raw ore mud feeding unit, this raw ore mud feeding unit connects the opening for feed of mud pulp equipment, and the discharge port of mud pulp equipment connects another opening for feed of large stock tank;
The discharge port of large stock tank connects ball mill, and ball mill is connected with spray-drying tower.
2. the continuous process for producing line of ceramic raw material stdn as claimed in claim 1, is characterized in that, these some sandstone feeding machines, for being arranged in parallel, form sandstone feeding unit.
3. the continuous process for producing line of ceramic raw material stdn as claimed in claim 1, is characterized in that, this sandstone feeding machine is provided with frequency conversion equipment, with quantitative load processed.
4. the continuous process for producing line of ceramic raw material stdn as claimed in claim 1, is characterized in that, this continuous ball milling unit is that some ball mills are staged connection.
5. the continuous process for producing line of ceramic raw material stdn as claimed in claim 4, is characterized in that, this ball mill is divided into three grades, and after one-level ball mill ball milling, slurry fineness is less than or equal to 0.4mm; After secondary ball mill ball milling, slurry fineness is less than or equal to 0.2mm; After three grades of ball mill ball millings, slurry fineness is less than or equal to 0.1mm.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201320789685.3U CN203558979U (en) | 2013-12-05 | 2013-12-05 | Standardized continuous treatment production line for ceramic raw materials |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201320789685.3U CN203558979U (en) | 2013-12-05 | 2013-12-05 | Standardized continuous treatment production line for ceramic raw materials |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN203558979U true CN203558979U (en) | 2014-04-23 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201320789685.3U Expired - Lifetime CN203558979U (en) | 2013-12-05 | 2013-12-05 | Standardized continuous treatment production line for ceramic raw materials |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103664195A (en) * | 2013-12-05 | 2014-03-26 | 广东萨米特陶瓷有限公司 | Standardized continuous treatment method of ceramic raw material and production line thereof |
| CN110204344A (en) * | 2019-05-21 | 2019-09-06 | 广东家美陶瓷有限公司 | Green body slurry and preparation method thereof |
-
2013
- 2013-12-05 CN CN201320789685.3U patent/CN203558979U/en not_active Expired - Lifetime
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103664195A (en) * | 2013-12-05 | 2014-03-26 | 广东萨米特陶瓷有限公司 | Standardized continuous treatment method of ceramic raw material and production line thereof |
| CN110204344A (en) * | 2019-05-21 | 2019-09-06 | 广东家美陶瓷有限公司 | Green body slurry and preparation method thereof |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CP01 | Change in the name or title of a patent holder | ||
| CP01 | Change in the name or title of a patent holder |
Address after: 528061 No.1 and No.2 Baitu village, Lubu Town, Gaoyao City, Zhaoqing City, Guangdong Province Patentee after: GUANGDONG SUMMIT CERAMICS Co.,Ltd. Patentee after: New Pearl Group Co.,Ltd. Address before: 528061 No.1 and No.2 Baitu village, Lubu Town, Gaoyao City, Zhaoqing City, Guangdong Province Patentee before: GUANGDONG SUMMIT CERAMICS Co.,Ltd. Patentee before: GUANGDONG NEWPEARL CERAMIC GROUP Co.,Ltd. |
|
| CP03 | Change of name, title or address | ||
| CP03 | Change of name, title or address |
Address after: 526124 Bai Tu Yi and ER Cun, Lubu Town, Gaoyao District, Zhaoqing City, Guangdong Province Patentee after: New Pearl (Guangdong) New Materials Co.,Ltd. Patentee after: New Pearl Group Co.,Ltd. Address before: 528061 No.1 and No.2 Baitu village, Lubu Town, Gaoyao City, Zhaoqing City, Guangdong Province Patentee before: GUANGDONG SUMMIT CERAMICS Co.,Ltd. Patentee before: New Pearl Group Co.,Ltd. |
|
| CX01 | Expiry of patent term | ||
| CX01 | Expiry of patent term |
Granted publication date: 20140423 |