CN203304270U - Polishing and raw material waste residue recovery system - Google Patents
Polishing and raw material waste residue recovery system Download PDFInfo
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- CN203304270U CN203304270U CN201320336106XU CN201320336106U CN203304270U CN 203304270 U CN203304270 U CN 203304270U CN 201320336106X U CN201320336106X U CN 201320336106XU CN 201320336106 U CN201320336106 U CN 201320336106U CN 203304270 U CN203304270 U CN 203304270U
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Abstract
The utility model discloses a polishing and raw material waste residue recovery system. A raw material residue water channel is connected with a raw material residue water pond; the raw material residue water pond is connected with a plurality of first concentration towers through pipelines; the first concentration towers are connected with a first transfer cylinder through pipelines; a vibration screen is arranged in the first transfer cylinder; the first transfer cylinder is connected with a first vacuum hydroextractor through a pipeline; the first vacuum hydroextractor is connected with a clear water pond through a pipeline and also connected with a waste residue recovery warehouse through a belt conveying device; a polishing residue water channel is connected with a polishing residue water pond; the polishing residue water pond is connected with a plurality of second concentration towers through the pipelines; the second concentration towers are connected with a second transfer cylinder through the pipelines; another vibration screen is arranged in the second transfer cylinder; the second transfer cylinder is connected with a second vacuum hydroextractor through the pipeline; the second vacuum hydroextractor is connected with the clear water pond through a pipeline and also connected with the waste residue recovery warehouse through a belt conveying device. The utility model provides the polishing and raw material waste residue recovery system.
Description
Technical field
The recovery system, particularly polishing slag of waste residue and the recovery system of raw material waste residue in the relevant a kind of ceramic industry of the utility model.
Background technology
At present, a large amount of solid waste contaminated environment not only in ceramic industry, and also the processing of waste material increased cost to manufacturer, and the recycling of waste residue has prospect widely.Waste residues of polished tiles is the waste residue of difficult utilization in current ceramic industry, it is also the waste residue that utilizes minimumly, but waste residues of polished tiles is a kind of good resource, the method of the recycling of waste residues of polished tiles is that (waste residues of polished tiles refers to that Imitation Rock Porcelain Tiles and thick glazed brick etc. are after scraping some row deep processings such as thicknessing, grinding and polishing and edging chamfering, a large amount of brick bits of generation by waste residues of polished tiles.According to production scene, understand, the grinding and polishing operation is removed the 0.5-0.7mm superficial layer by the adobe surface usually, and what have even needs jettisoning 1-2mm superficial layer.Every generation 1m
2Polished bricks, will produce the brick bits of 1.5kg left and right, the wearing and tearing of cutter and grinding tool simultaneously also produce the chip of 0.5kg left and right, the about 2kg of gross weight) by it, whether contact the polishing abrading block and be divided into two large class: A, the waste residues of polished tiles of not contacted polishing abrading block (edging namely, strike off, the slag that rear edging produces, account for 70% of waste residue total amount, this waste residue does not foam in sintering process) can be according to the 10-25%(weight ratio) quantity add backing material formula to make powder (do bed material with), for the production of micro mist polished brick in porcelain character (doing bed material).By the classified use to waste residue, can accomplish fully twice laid, realize that clean energy resource recycles, and reduces production costs; Washing ball and give the floor a flush and produce large content of starting materials waste water when rinse water coal slurry tower after B, ceramic ball mill raw materials for production, the raw material waste residue after collection can be re-used as bed material and use after the ball milling refinement.
The recycling of learning in sum polishing and raw material waste residue is very important.
The utility model content
The technical problem that the utility model solves is namely providing a kind of system that above-mentioned polishing slag and raw material waste residue are reclaimed.
The technological means that the utility model adopts is as described below.
A kind of polishing and raw material waste residue recovery system, it comprises raw material pulp water raceway groove and polishing pulp water raceway groove, this raw material pulp water raceway groove connects raw material pulp water pond, this raw material pulp water pond connects some the first concentration towers by pipeline, this first concentration tower connects the first transferring cylinder by pipeline, is provided with riddler in this first transferring cylinder; This first transferring cylinder connects the first vacuum hydroextractor by pipeline; This first vacuum hydroextractor connects clear water reserviors by pipeline, and this first vacuum hydroextractor also connects waste residue by belt conveyor and reclaims warehouse; This polishing pulp water raceway groove connects polishing pulp water pond, and this polishing pulp water pond connects some the second concentration towers by pipeline, and this second concentration tower connects the second transferring cylinder by pipeline, is provided with riddler in this second transferring cylinder; This second transferring cylinder connects the second vacuum hydroextractor by pipeline; This second vacuum hydroextractor connects clear water reserviors by pipeline, and this second vacuum hydroextractor also connects waste residue by belt conveyor and reclaims warehouse.
Each first concentration tower is connected in parallel, and each second concentration tower is connected in parallel.
This first concentration tower is 3 groups and is arranged in parallel, and this second concentration tower is 4 groups and is arranged in parallel.
This first concentration tower is connected with clear water reserviors by pipeline with the second concentration tower.
Between this raw material pulp water pond and the first concentration tower, be provided with slush pump; Between this polishing pulp water pond and the second concentration tower, be provided with slush pump.
Between this first transferring cylinder and the first vacuum hydroextractor, be provided with slush pump; Between this second transferring cylinder and the second vacuum hydroextractor, be provided with slush pump.
The beneficial effect that the utility model produces is as follows: 1, the waste residue rate of recovery of polishing and raw material waste residue recovery system reaches more than 75%; 2, input cost is lower, and output is high: the disposable input of all devices is about 1,370,000 yuan, and output is annual more than 500 ten thousand yuan (polishing and raw material waste residue are made ceramic raw material); 3, equipment operating is easy to maintenance: only 1-2 name operative employee just can operation and maintenance; 4, reduce the waste residue treating capacity in environmental protection pond; 5, alleviate sanitationman's labour intensity, 6, reduce the consumption of the heavy agent of speed.
The accompanying drawing explanation
Fig. 1 is polishing of the present utility model and raw material waste residue recovery system schematic diagram.
The specific embodiment
As shown in Figure 1, a kind of polishing of the utility model and raw material waste residue recovery system, it comprises raw material pulp water raceway groove 1 and polishing pulp water raceway groove 3, this raw material pulp water raceway groove 1 connects raw material pulp water pond 2, this raw material pulp water pond 2 connects some the first concentration towers 71 by pipeline 5, this first concentration tower 71 connects the first transferring cylinder 81 by pipeline, is provided with riddler in this first transferring cylinder 81; This first transferring cylinder 81 connects the first vacuum hydroextractor 101 by pipeline; This first vacuum hydroextractor 101 connects clear water reserviors 9 by pipeline, and this first vacuum hydroextractor 101 also connects waste residue by belt conveyor 11 and reclaims warehouse 12.
This polishing pulp water raceway groove 3 connects polishing pulp water pond 4, and this polishing pulp water pond 4 connects some the second concentration towers 72 by pipeline 5, and this second concentration tower 72 connects the second transferring cylinder 82 by pipeline, is provided with riddler in this second transferring cylinder 82; This second transferring cylinder 82 connects the second vacuum hydroextractor 102 by pipeline; This second vacuum hydroextractor 102 connects clear water reserviors 9 by pipeline, and this second vacuum hydroextractor 102 also connects waste residue by belt conveyor 11 and reclaims warehouse 12.
As shown in Figure 1, this first concentration tower is 3 groups and is arranged in parallel, and this second concentration tower is 4 groups and is arranged in parallel, and this first concentration tower is connected with clear water reserviors by pipeline with the second concentration tower.And, between raw material pulp water pond and polishing pulp water pond and first, second concentration tower, slush pump can also be set; Between this first, second transferring cylinder and first, second vacuum hydroextractor, also slush pump can be set.
Below with the embodiment of Fig. 1, its recovery operation method is described.
A, original raw material pulp water raceway groove 1 and polishing pulp water raceway groove 3 are carried out to layout again: respectively the waste residue water of polishing (front edging, strike off, rear edging waste residue) and raw material (wash ball and rush floor and the waste residue of rinse water coal slurry tower) is guided to the processing of classifying of corresponding raw material pulp water pond 2 and polishing pulp water pond 4.
B, by pipeline 5 and slush pump 6, waste residue water is pumped into to first, second concentration tower 71,72 and concentrate, pulp water concentration reaches the 30%(mass fraction) when above, pulp water flows automatically to first, second transferring cylinder 81,82(contains riddler, and riddler is by the heavy particulate leaching in pulp water).
C, slush pump 6 carry out vacuum dehydration to the pulp water pump of higher concentration in first, second transferring cylinder 81,82 to first, second vacuum hydroextractor 101,102, are less than the 25%(mass fraction thereby obtain moisture content) waste residue.
D, by belt conveyer 11, waste residue being transported to waste residue, to reclaim warehouse 12 stand-by.
The clear water that the clear water that E, first, second vacuum hydroextractor processing pulp water obtain and concentration tower overflow flows automatically to clear water reserviors 9 and carries out cycling and reutilization.
Claims (6)
1. a polishing and raw material waste residue recovery system, it comprises raw material pulp water raceway groove and polishing pulp water raceway groove, it is characterized in that:
This raw material pulp water raceway groove connects raw material pulp water pond, and this raw material pulp water pond connects some the first concentration towers by pipeline, and this first concentration tower connects the first transferring cylinder by pipeline, is provided with riddler in this first transferring cylinder; This first transferring cylinder connects the first vacuum hydroextractor by pipeline; This first vacuum hydroextractor connects clear water reserviors by pipeline, and this first vacuum hydroextractor also connects waste residue by belt conveyor and reclaims warehouse;
This polishing pulp water raceway groove connects polishing pulp water pond, and this polishing pulp water pond connects some the second concentration towers by pipeline, and this second concentration tower connects the second transferring cylinder by pipeline, is provided with riddler in this second transferring cylinder; This second transferring cylinder connects the second vacuum hydroextractor by pipeline; This second vacuum hydroextractor connects clear water reserviors by pipeline, and this second vacuum hydroextractor also connects waste residue by belt conveyor and reclaims warehouse.
2. polishing as claimed in claim 1 and raw material waste residue recovery system, is characterized in that, each first concentration tower is connected in parallel, and each second concentration tower is connected in parallel.
3. polishing as claimed in claim 1 and raw material waste residue recovery system, is characterized in that, this first concentration tower is 3 groups and is arranged in parallel, and this second concentration tower is 4 groups and is arranged in parallel.
4. polishing as claimed in claim 1 and raw material waste residue recovery system, is characterized in that, this first concentration tower is connected with clear water reserviors by pipeline with the second concentration tower.
5. polishing as claimed in claim 1 and raw material waste residue recovery system, is characterized in that, is provided with slush pump between this raw material pulp water pond and the first concentration tower; Between this polishing pulp water pond and the second concentration tower, be provided with slush pump.
6. polishing as claimed in claim 5 and raw material waste residue recovery system, is characterized in that, is provided with slush pump between this first transferring cylinder and the first vacuum hydroextractor; Between this second transferring cylinder and the second vacuum hydroextractor, be provided with slush pump.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201320336106XU CN203304270U (en) | 2013-06-13 | 2013-06-13 | Polishing and raw material waste residue recovery system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201320336106XU CN203304270U (en) | 2013-06-13 | 2013-06-13 | Polishing and raw material waste residue recovery system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN203304270U true CN203304270U (en) | 2013-11-27 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201320336106XU Withdrawn - After Issue CN203304270U (en) | 2013-06-13 | 2013-06-13 | Polishing and raw material waste residue recovery system |
Country Status (1)
| Country | Link |
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| CN (1) | CN203304270U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103331290A (en) * | 2013-06-13 | 2013-10-02 | 广东新明珠陶瓷集团有限公司 | Recovery system and method for polishing and raw material waste residue |
-
2013
- 2013-06-13 CN CN201320336106XU patent/CN203304270U/en not_active Withdrawn - After Issue
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103331290A (en) * | 2013-06-13 | 2013-10-02 | 广东新明珠陶瓷集团有限公司 | Recovery system and method for polishing and raw material waste residue |
| CN103331290B (en) * | 2013-06-13 | 2015-08-19 | 广东新明珠陶瓷集团有限公司 | Polishing and raw material waste residue recovery system and method |
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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: 20131127 Effective date of abandoning: 20150819 |
|
| RGAV | Abandon patent right to avoid regrant |