CN203754528U - Device for treating waste water during production of glass - Google Patents
Device for treating waste water during production of glass Download PDFInfo
- Publication number
- CN203754528U CN203754528U CN201420052601.2U CN201420052601U CN203754528U CN 203754528 U CN203754528 U CN 203754528U CN 201420052601 U CN201420052601 U CN 201420052601U CN 203754528 U CN203754528 U CN 203754528U
- Authority
- CN
- China
- Prior art keywords
- waste water
- tank
- coagulation reaction
- reaction tank
- glass
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Fee Related
Links
- 239000002351 wastewater Substances 0.000 title claims abstract description 65
- 239000011521 glass Substances 0.000 title claims abstract description 25
- 238000004519 manufacturing process Methods 0.000 title claims abstract description 17
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 47
- 238000006243 chemical reaction Methods 0.000 claims abstract description 35
- 238000005345 coagulation Methods 0.000 claims abstract description 35
- 230000015271 coagulation Effects 0.000 claims abstract description 35
- 238000004062 sedimentation Methods 0.000 claims abstract description 18
- 239000010802 sludge Substances 0.000 claims abstract description 18
- 238000000227 grinding Methods 0.000 abstract description 10
- 238000000034 method Methods 0.000 abstract description 7
- 238000004065 wastewater treatment Methods 0.000 abstract description 6
- 230000000694 effects Effects 0.000 abstract description 2
- 239000010842 industrial wastewater Substances 0.000 abstract description 2
- 238000007599 discharging Methods 0.000 abstract 3
- 238000001914 filtration Methods 0.000 description 7
- 238000005516 engineering process Methods 0.000 description 4
- 238000001556 precipitation Methods 0.000 description 3
- 238000004140 cleaning Methods 0.000 description 2
- 239000006063 cullet Substances 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 238000003912 environmental pollution Methods 0.000 description 1
- 238000011010 flushing procedure Methods 0.000 description 1
- 239000010808 liquid waste Substances 0.000 description 1
- 239000012528 membrane Substances 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 239000013618 particulate matter Substances 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- 238000011084 recovery Methods 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
Landscapes
- Separation Of Suspended Particles By Flocculating Agents (AREA)
Abstract
The utility model discloses a device for treating waste water, produced in a grinding process of a glass production line, during production of glass and belongs to the technical field of industrial waste water treatment. The device for treating the waste water during the production of the glass comprises a waste water tank, a water collecting tank, a mud pump, a coagulation reaction tank and a clear water tank, wherein the waste water tank is connected with the water collecting tank through the waste water pump, an outlet of the coagulation reaction tank is connected with an inlet of the clear water tank by virtue of a valve connecting pipe; the device for treating the waste water during the production of the glass also comprises a sludge tank and a box type filter press, a sludge discharging pipe is arranged at the outlet of the coagulation reaction tank, the coagulation reaction tank is connected with the sludge tank by virtue of the sludge discharging pipe, and the sludge discharging pipe is connected with the box type filter press. According to the device for treating the waste water during the production of the glass, waste water is sedimented twice and the sedimentation effect is more sufficient; compared with a waste water treatment system in the prior art, the device for treating the waste water during the production of the glass has the advantages that the waste water is effectively treated and recycled, and sludge is recycled after being sedimented and is not discharge outside, so that resource is saved, and no pollution to the environment is caused.
Description
Technical field
The utility model relates to technology for treating industrial waste water field, is particularly a kind ofly grinding and the treatment unit of the glass production waste water that produces of cleaning process for glass production line.
Background technology
In the grinding of glass production line and cleaning process, can produce a lot of waste water, in waste water, contain the suspended substances such as a large amount of cullet.This type of waste water is mainly that SS concentration is higher, and water quality, the water yield situation of waste water are as follows:
If the waste water and the mud that produce directly discharge, both pollute environment, also waste water resources.
Granted publication number is that the utility model of CN202449928U discloses a kind of glass grinding Waste Water Treatment, comprises the glass grinding wastewater collection and body refuse press filtration unit, a filtering separation unit and reuse water collection and the back flushing unit that connect successively.This utility model has can effectively process glass grinding waste water, can effectively filter 99. 6% particulate matter, the advantage of the turbidity of effluent quality below 5NTU after processing.
In the disclosed abolishment treatment system of this utility model, waste water through settling tank processing is pumped by the wastewater discharge pipe at glass grinding wastewater disposal basin middle part by waste water pump, then enter in clean water basin through the processing of tubular membrane water treatment unit, waste water can recycle through processing.But its weak point is, after purification tank for liquid waste, after waste water is pulled out, remaining mud cannot be cleared up, and can not reclaim comprehensive utilization, cause and pollute and waste.
Utility model content
The purpose of this utility model is to overcome the deficiencies in the prior art, the treatment unit of the glass grinding waste water of the useless tiny particle in water of a kind of effective removal glass grinding is provided, not only can make waste water in whole technology for making glass can effectively process recovery, and comprehensive utilization is also cleared up and reclaim to mud in the lump, this apparatus structure is simple, and wastewater treatment rate is high.
Above-mentioned technical purpose of the present utility model is achieved by the following technical programs:
A kind for the treatment of unit of glass production waste water, comprise wastewater disposal basin, water collecting basin, slush pump, coagulation reaction tank, clean water basin, described wastewater disposal basin middle part is provided with wastewater discharge pipe, described wastewater discharge pipe connects the muddy water tail pipe of described water collecting basin by a waste water pump, the vent pipe of described water collecting basin connects the entrance of described coagulation reaction tank by described slush pump, the outlet of described coagulation reaction tank is connected by valve pipe connecting with the entrance of described clean water basin, it is characterized in that: also comprise sludge sump and chamber-type press filter, the outlet of described coagulation reaction tank is provided with mud vent pipe, described coagulation reaction tank is connected with described sludge sump by mud vent pipe, described sludge sump vent pipe is connected with described chamber-type press filter.
As preferably, between described coagulation reaction tank and clean water basin, be also provided with settling tank, described waste water, after described coagulation reaction tank is processed, enters and after described settling tank is processed, enters clean water basin again and carry out reuse.
As preferably, between described water collecting basin and described coagulation reaction tank, be also provided with preliminary sedimentation tank, the waste water after the sedimentation and filtration for the first time of preliminary sedimentation tank enters water collecting basin, after slush pump and coagulation reaction tank, again enter settling tank, twice sedimentation and filtration is more abundant.
As preferably, described preliminary sedimentation tank and described coagulation reaction tank be connected respectively to plate-and-frame filter press.Plate-and-frame filter press can a large amount of mud of continuous filter press, and dewatering efficiency is high.
In sum, the wastewater treatment of this utility model is because through twice precipitation, and effect is more abundant; And Waste Water Treatment compared to existing technology, not only can effectively process waste water and recycle, and can be simultaneously by mud after precipitation process, recycle, externally discharge, had not both saved resource, and had not caused environmental pollution.
Brief description of the drawings
Fig. 1 is structural representation of the present utility model;
In figure, 1, wastewater disposal basin; 11, wastewater discharge pipe; 12, waste water pump; 2, water collecting basin; 21, muddy water tail pipe; 22, the vent pipe of water collecting basin; 3, slush pump; 4, coagulation reaction tank; 41, mud vent pipe; 5, clean water basin; 6, sludge sump; 7, chamber-type press filter; 8, settling tank; 9, preliminary sedimentation tank; 10, plate-and-frame filter press.
Embodiment
Below in conjunction with accompanying drawing, the utility model is described in further detail.
Embodiment: as shown in Figure 1, a kind for the treatment of unit of glass production waste water, comprise wastewater disposal basin 1, water collecting basin 2, slush pump 3, coagulation reaction tank 4, clean water basin 5, described wastewater disposal basin 1 middle part is provided with wastewater discharge pipe 11, described wastewater discharge pipe 11 connects the muddy water tail pipe 21 of described water collecting basin 2 by a waste water pump 12, the vent pipe 22 of described water collecting basin connects the entrance of described coagulation reaction tank 4 by described slush pump 3, between coagulation reaction tank 4 and clean water basin 5, be also provided with settling tank 8, the outlet of described coagulation reaction tank 4 is connected by valve pipe connecting with the entrance of described clean water basin 5 by settling tank 8 is rear, also comprise sludge sump 6 and chamber-type press filter 7, the outlet of described coagulation reaction tank 4 is provided with mud vent pipe 41, described coagulation reaction tank 4 is connected with described sludge sump 6 by mud vent pipe 41, described sludge sump 6 vent pipes are connected with described chamber-type press filter 7.
Waste water, after coagulation reaction tank 4 is processed, enters and after settling tank 8 is processed, enters clean water basin 5 again and carry out reuse.
Between water collecting basin 2 and coagulation reaction tank 4, be also provided with preliminary sedimentation tank 9, the waste water after the sedimentation and filtration for the first time of preliminary sedimentation tank 9 enters water collecting basin, after slush pump and coagulation reaction tank, again enters settling tank, and twice sedimentation and filtration is more abundant.
Preliminary sedimentation tank 9 and described coagulation reaction tank 4 be connected respectively to plate-and-frame filter press 10.
When processing, first glass grinding waste water is collected by the collecting gutter in workshop, flowed into wastewater disposal basin 1, waste water pumps into water collecting basin 2 through wastewater discharge pipe 11 by waste water pump 12; Waste water in water collecting basin 2 pumps into preliminary sedimentation tank 9, after the first step sedimentation and filtration of preliminary sedimentation tank 9, pump into coagulation reaction tank 4 by slush pump 3, in pond, regulate the pH of waste water to be controlled between 7-8, after mixing, add PAC, PAM, the cohesion of deposit seeds thing is become and be easy to greatly precipitation; Coagulation reaction tank 4 water outlets enter settling tank 8, carry out secondary sedimentation, and mud enters sludge sump 6.The discharge water of settling tank 8 enters clean water basin 5 and recycles; The mud of sludge sump 6 is recycled by 7 times equalizing tanks of chamber-type press filter after processing by chamber-type press filter 7.
Claims (4)
1. the treatment unit of a glass production waste water, comprise wastewater disposal basin (1), water collecting basin (2), slush pump (3), coagulation reaction tank (4), clean water basin (5), described wastewater disposal basin (1) middle part is provided with wastewater discharge pipe (11), described wastewater discharge pipe (11) connects the muddy water tail pipe (21) of described water collecting basin (2) by a waste water pump (12), the vent pipe (22) of described water collecting basin connects the entrance of described coagulation reaction tank (4) by described slush pump (3), the outlet of described coagulation reaction tank (4) is connected by valve pipe connecting with the entrance of described clean water basin (5), it is characterized in that: also comprise sludge sump (6) and chamber-type press filter (7), the outlet of described coagulation reaction tank (4) is provided with mud vent pipe (41), described coagulation reaction tank (4) is connected with described sludge sump (6) by mud vent pipe (41), described sludge sump (6) vent pipe is connected with described chamber-type press filter (7).
2. the treatment unit of a kind of glass production waste water according to claim 1, is characterized in that: between described coagulation reaction tank (4) and clean water basin (5), be also provided with settling tank (8).
3. the treatment unit of glass production waste water according to claim 2, is characterized in that: between described water collecting basin (2) and described coagulation reaction tank (4), be also provided with preliminary sedimentation tank (9).
4. the treatment unit of glass production waste water according to claim 3, is characterized in that: described preliminary sedimentation tank (9) and described coagulation reaction tank (4) be connected respectively to plate-and-frame filter press (10).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420052601.2U CN203754528U (en) | 2014-01-27 | 2014-01-27 | Device for treating waste water during production of glass |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420052601.2U CN203754528U (en) | 2014-01-27 | 2014-01-27 | Device for treating waste water during production of glass |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN203754528U true CN203754528U (en) | 2014-08-06 |
Family
ID=51249827
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201420052601.2U Expired - Fee Related CN203754528U (en) | 2014-01-27 | 2014-01-27 | Device for treating waste water during production of glass |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN203754528U (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112794604A (en) * | 2021-01-19 | 2021-05-14 | 上海秦望环保材料有限公司 | Sludge treatment device with high solid recovery |
| CN113735380A (en) * | 2021-09-23 | 2021-12-03 | 襄阳鑫明宇光电科技有限公司 | Method for recycling and treating optical glass part processing wastewater |
| CN117326602A (en) * | 2023-09-11 | 2024-01-02 | 山东温声玻璃科技股份有限公司 | Wastewater circulation system for glass production and working method thereof |
-
2014
- 2014-01-27 CN CN201420052601.2U patent/CN203754528U/en not_active Expired - Fee Related
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112794604A (en) * | 2021-01-19 | 2021-05-14 | 上海秦望环保材料有限公司 | Sludge treatment device with high solid recovery |
| CN113735380A (en) * | 2021-09-23 | 2021-12-03 | 襄阳鑫明宇光电科技有限公司 | Method for recycling and treating optical glass part processing wastewater |
| CN117326602A (en) * | 2023-09-11 | 2024-01-02 | 山东温声玻璃科技股份有限公司 | Wastewater circulation system for glass production and working method thereof |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20140806 Termination date: 20190127 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |