CN208087432U - A kind of glass production effluent cycle reuse means - Google Patents
A kind of glass production effluent cycle reuse means Download PDFInfo
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- CN208087432U CN208087432U CN201820959403.2U CN201820959403U CN208087432U CN 208087432 U CN208087432 U CN 208087432U CN 201820959403 U CN201820959403 U CN 201820959403U CN 208087432 U CN208087432 U CN 208087432U
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- collecting
- tank
- glass production
- filtering ponds
- reuse means
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Abstract
The utility model provides a kind of glass production effluent cycle reuse means, including the first collecting-tank, second collecting-tank, sedimentation basin, filtering ponds and return water pond, the first collecting-tank water inlet is equipped with flase floor, water outlet is connected with the second collecting-tank, first collecting-tank is also pumped with coagulant dosage by pipeline respectively, dosing pump is connected, agitating device is equipped in second collecting-tank, the second collecting-tank water outlet passes through pipeline and sedimentation basin, filtering ponds are sequentially connected, MBR membrane biological reaction apparatus is equipped in the filtering ponds, positive suction pump is equipped between the filtering ponds and return water pond, reverse cleaning pumps.The utility model enormously simplifies the sewage disposal in glass production by the immixture of MBR membrane biological reaction apparatus and coagulant dosage pump, dosing pump, agitating device, so that glass production sewage is realized Ke Xunhuanliyong.
Description
Technical field
The utility model is related to technical field of industrial sewage treatment more particularly to a kind of glass production effluent cycle to recycle
Device.
Background technology
Glass industry can directly or indirectly discharge various wastewater in process of production, and wherein treating capacity maximum, fund is thrown
It is abrasive waste water processing to enter maximum, and glass grinding waste water mainly contains a large amount of glass fine powder particle, these particles are mostly with outstanding
Floading condition form is present in waste water, although the clean-up performance of the water of this part makes a big difference with tap water, only need by
After glass powder filtering in waste water, so that it may be used with recirculating, in existing glass processing enterprise, will usually contain glass powder
The direct discharging of waste water at end, not only considerably increases the production cost of enterprise, also easily pollutes the environment.
Utility model content
The purpose of this utility model is to provide a kind of glass production effluent cycle reuse means, to solve above-mentioned background
The problem of being proposed in technology.
The utility model is achieved through the following technical solutions：A kind of glass production effluent cycle reuse means, packet
The first collecting-tank, the second collecting-tank, sedimentation basin, filtering ponds and return water pond are included, the first collecting-tank water inlet is equipped with
Flase floor, water outlet are connected with the second collecting-tank, the first collecting-tank also by pipeline respectively with coagulant dosage pump, dosing
Pump is connected, and agitating device is equipped in second collecting-tank, and the second collecting-tank water outlet passes through pipeline and sedimentation basin, mistake
Filter tank is sequentially connected, and MBR membrane biological reaction apparatus is equipped in the filtering ponds, and forward direction is equipped between the filtering ponds and return water pond
Suction pump, reverse cleaning pump.
Preferably, the water outlet of the MBR membrane biological reaction apparatus is connected by positive suction pump with return water with pond, described
The water outlet of MBR membrane biological reaction apparatus is also pumped by reverse cleaning to be connected with the first collecting-tank.
Preferably, the agitating device is frequency control blender.
Preferably, the bottom of the sedimentation basin is equipped with residual cake valve, and the residual cake valve is connected with sediment collecting box.
Preferably, the filtering ponds bottom is equipped with aeration opening, and the aeration opening is connected by blowing line with wind turbine.
Preferably, the wind turbine is Roots blower.
Compared with prior art, what the utility model reached has the beneficial effect that：A kind of glass provided by the utility model
Production waste circulation recycling device can be reacted by dispensing coagulant dosage pump, dosing pump, make the glass powder in sewage
End can precipitate, while the agitating device by being arranged in the first collecting-tank, the second collecting-tank, can effectively improve reaction
Time, the sewage after reacting are filtered by MBR membrane reactors, and filtered water can re-apply in glass production,
Greatly reduce the environmental pollution in glass production.
Description of the drawings
It is required in being described below to embodiment in order to illustrate more clearly of the technical scheme in the embodiment of the utility model
Attached drawing to be used is briefly described, it should be apparent that, the accompanying drawings in the following description is only the preferred reality of the utility model
Example is applied, it for those of ordinary skill in the art, without having to pay creative labor, can also be attached according to these
Figure obtains other attached drawings.
Fig. 1 is a kind of structure chart of glass production effluent cycle reuse means provided by the utility model.
In figure.The first collecting-tanks of 1-, the second collecting-tanks of 2-, 3- sedimentation basins, 4- filtering ponds, 5- return water pond, 6- flase floors,
7- coagulant dosages pump, 8- dosing pumps, 9- pipelines, 10- residual cake valves, 11- sediment collecting boxs, 12-MBR membrane biological reactions dress
It sets, 13- Roots blowers, 14- agitating devices, 15- forward direction suction pumps, 16- reverse cleanings pump, 17- blowing lines.
Specific implementation mode
In order to be best understood from the utility model technology contents, specific embodiment is provided below, and in conjunction with attached drawing to this practicality
It is novel to be described further.
Referring to Fig. 1, a kind of glass production effluent cycle reuse means, including it is the first collecting-tank 1, the second collecting-tank 2, heavy
Shallow lake pond 3, filtering ponds 4 and return water pond 5,1 water inlet of the first collecting-tank are equipped with flase floor 6, and flase floor 6 may filter that greatly
The sundries such as particle glass chip, 1 water outlet of the first collecting-tank are connected with the second collecting-tank 2, and the first collecting-tank 1 also passes through pipeline
9 are connected with coagulant dosage pump 7, dosing pump 8 respectively, and coagulant is added into the first collecting-tank 1 in coagulant dosage pump 7, adds
Lime is added into the first collecting-tank 1 for Teat pipette 8, and agitating device 14, second collecting-tank 2 are equipped in second collecting-tank 2
Water outlet is sequentially connected by pipeline 9 and sedimentation basin 3, filtering ponds 4, and MBR membrane biological reaction apparatus is equipped in the filtering ponds 4
12, the filtering ponds 4 and return water pump 16 between pond 5 equipped with positive suction pump 15, reverse cleaning.
Specifically, the water outlet of the MBR membrane biological reaction apparatus 12 passes through positive suction pump 15 and return water 5 phase of pond
Even, filtered water is evacuated to carrying out secondary use, the MBR membrane biological reactions in pond 5 by return water by positive suction pump 15
The water outlet of device 12 is also connected by reverse cleaning pump 16 with the first collecting-tank 1, can be given birth to MBR films by reverse cleaning pump 16
Object reaction unit 12 is cleaned, and the sewage after cleaning flows into the first collecting-tank 1 and re-starts reaction.
Specifically, the agitating device 14 is frequency control blender, reaction can be accelerated by frequency control blender
Rate.
Specifically, 3 bottom of the sedimentation basin is equipped with residual cake valve 10, precipitation can be sent the material of precipitation by opening residual cake valve 10
It is further processed in object collecting box 11.
Specifically, 4 bottom of the filtering ponds is equipped with aeration opening, the aeration opening passes through blowing line 17 and Roots blower
13 are connected, to provide air for the biochemical treatment of MBR membrane biological reaction apparatus 12.
Operation principle is：Sewage in glass production is from workshop the first collecting-tank 11 of inflow, the first collecting-tank 1
Flase floor 6 retains the sundries such as the bulky grain glass chip in sewage, opens coagulant dosage pump 7, dosing pump 8, catchments to first
It is separately added into the medicaments such as coagulant and lime in pond 1, the sewage being added after medicament flows into the second collecting-tank 2, in the second collecting-tank 2
Frequency control blender is stirred sewage, improves the rate that reaction carries out, and the sewage after reaction, which flows into sedimentation basin 3, to carry out
It further staticly settles, the bottom material after precipitation is sent by residual cake valve 10 in sediment collecting box 11, and the sewage on upper layer flows again
Enter in filtering ponds 4, through in filtering ponds 4 MBR membrane biological reaction apparatus 12 filter after, by positive suction pump 15 aspirate filtrate from
The water outlet of MBR membrane biological reaction apparatus 12 is flow in return water pond 5, according to the cleaning requirement of MBR membrane biological reaction apparatus 12,
Positive suction pump 15 stops after working 1 to 3 month, starts reverse cleaning 16 pairs of MBR membrane biological reaction apparatus 12 of pump and carries out instead clearly
It washes, the sewage after anti-cleaning, which back flows back into the first collecting-tank 1, to be reacted, and is ensured filtered water water quality good stable, is returned
Water is supplied water by pipeline 9 to glass processing workshop with the water in pond 5, is realized the recycling of glass production sewage, is avoided polluting
Environment.
The above is only the preferred embodiment of the utility model only, is not intended to limit the utility model, all at this
Within the spirit and principle of utility model, any modification, equivalent substitution, improvement and etc. done should be included in the utility model
Within the scope of protection.
Claims (6)
1. a kind of glass production effluent cycle reuse means, which is characterized in that including the first collecting-tank, the second collecting-tank, sink
Shallow lake pond, filtering ponds and return water pond, the first collecting-tank water inlet are equipped with flase floor, water outlet and the second collecting-tank
It is connected, the first collecting-tank is also connected with coagulant dosage pump, dosing pump by pipeline respectively, is set in second collecting-tank
There are agitating device, the second collecting-tank water outlet to be sequentially connected by pipeline and sedimentation basin, filtering ponds, set in the filtering ponds
There is MBR membrane biological reaction apparatus, positive suction pump, reverse cleaning pump are equipped between the filtering ponds and return water pond.
2. a kind of glass production effluent cycle reuse means according to claim 1, which is characterized in that the MBR films
The water outlet of biological reaction apparatus is connected by positive suction pump with return water with pond, the water outlet of the MBR membrane biological reaction apparatus
Mouth is also pumped by reverse cleaning to be connected with the first collecting-tank.
3. a kind of glass production effluent cycle reuse means according to claim 1, which is characterized in that the stirring dress
It is set to frequency control blender.
4. a kind of glass production effluent cycle reuse means according to claim 1, which is characterized in that the sedimentation basin
Bottom be equipped with residual cake valve, the residual cake valve is connected with sediment collecting box.
5. a kind of glass production effluent cycle reuse means according to claim 1, which is characterized in that the filtering ponds
Bottom is equipped with aeration opening, and the aeration opening is connected by blowing line with wind turbine.
6. a kind of glass production effluent cycle reuse means according to claim 5, which is characterized in that the wind turbine is
Roots blower.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201820959403.2U CN208087432U (en) | 2018-06-22 | 2018-06-22 | A kind of glass production effluent cycle reuse means |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201820959403.2U CN208087432U (en) | 2018-06-22 | 2018-06-22 | A kind of glass production effluent cycle reuse means |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN208087432U true CN208087432U (en) | 2018-11-13 |
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ID=64053134
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201820959403.2U Active CN208087432U (en) | 2018-06-22 | 2018-06-22 | A kind of glass production effluent cycle reuse means |
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| Country | Link |
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| CN (1) | CN208087432U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113931689A (en) * | 2021-11-11 | 2022-01-14 | 重庆大学 | Drainage and purification system and method for reverse slope tunnel |
-
2018
- 2018-06-22 CN CN201820959403.2U patent/CN208087432U/en active Active
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113931689A (en) * | 2021-11-11 | 2022-01-14 | 重庆大学 | Drainage and purification system and method for reverse slope tunnel |
| CN113931689B (en) * | 2021-11-11 | 2024-03-22 | 重庆大学 | Reverse slope tunnel drainage and purification system and method |
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