CN206447735U - A kind of sewerage integrated processing system - Google Patents
A kind of sewerage integrated processing system Download PDFInfo
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- CN206447735U CN206447735U CN201720097619.8U CN201720097619U CN206447735U CN 206447735 U CN206447735 U CN 206447735U CN 201720097619 U CN201720097619 U CN 201720097619U CN 206447735 U CN206447735 U CN 206447735U
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Abstract
The utility model discloses a kind of sewerage integrated processing system, it is characterised in that：Including a biochemical treatment system, for being handled for the first time in biochemical mode raw sewage；One intermediate water reuse system, it is communicated in the biochemical treatment system, the intermediate water reuse system is used to carry out after-treatment to the waste water after the biochemical treatment system for the first time processing, obtains regenerative wastewater and preliminary purification water, and regenerative wastewater is back into the biochemical treatment system；One chemical phosphorus removal system, is communicated in the intermediate water reuse system, and the chemical phosphorus removal system is used to handle the preliminary purification water, obtains discharging water；One medicine system, the various reagents for adding processing waste water for the biochemical treatment system, intermediate water reuse system and chemical phosphorus removal system.
Description
Technical field
The utility model is related to field of waste water treatment, specially a kind of sewerage integrated processing system.
Background technology
During the manufacturing, waste water generation is had, these waste water how are handled, be that current needs are paid attention to and studied
Problem.Particularly with regard to sodium nitrate waste water, sodium sulfate wastewater, paper waste, sodium chloride waste water in inorganic chemical industry industry etc.；
Organic chemical industry's industry：Dyestuff, synthesis, food, pharmacy etc.；Smelting industry：Steel-making, nickel ore concentrate powder, iron concentrate powder, tar dephenolize
Deng；Other：Mud waste water, slag and effluent, etc..
With the increasingly quickening of industrialized production, environmental protection and water resource recycle and have put on new schedule.At present,
Though there are many Waste Water Treatments, involve great expense mostly, and the requirement to equipment is too high, and occupied ground area is big.Due to
The presence of these problems, existing factory is difficult to configure more applicable Waste Water Treatment, and causes environmental pollution increasingly tight
Weight.And the existing easy processing system of waste water, wastewater treatment do not reach the requirement reused, it is difficult to by the waste water after processing
Recovery is reused, and can cause the increase of production cost.Moreover, existing Waste Water Treatment is merely able to make letter to waste water
Single processing, is unable to circular treatment, does not reach environmental requirement.
The content of the invention
The purpose of this utility model is：A kind of sewerage integrated processing system is provided, is capable of the integrated circulation of system
Handle waste water.
Realizing the technical scheme of above-mentioned purpose is：A kind of sewerage integrated processing system, including
One biochemical treatment system, for being handled for the first time in biochemical mode raw sewage；
One intermediate water reuse system, is communicated in the biochemical treatment system, and the intermediate water reuse system is used for the biochemistry
Waste water after processing system processing for the first time carries out after-treatment, obtains regenerative wastewater and preliminary purification water, and regenerative wastewater is returned
It is back to the biochemical treatment system；
One chemical phosphorus removal system, is communicated in the intermediate water reuse system, and the chemical phosphorus removal system is used for described preliminary
Purified water is handled, and obtains discharging water；
One medicine system, at for the biochemical treatment system, intermediate water reuse system and chemical phosphorus removal system addition
Manage the various reagents of waste water.
The biochemical treatment system includes
One regulating reservoir, the various waste water of processing needed for for adjusting distribution；
One anaerobic pond, for the waste water extracted in a upper processing pond and the partial organic substances removed in the waste water；
An at least anoxic pond, it is organic for the waste water extracted after the anaerobic pond processing and the part removed in the waste water
Thing；
An at least Aerobic Pond, for the organic matter in the waste water after being handled through a upper processing pond that digests, degrades；
One sedimentation basin, for storing, precipitating the waste water after the anaerobic pond, anaerobic pond, Aerobic Pond processing, and will be heavy
The waste water in shallow lake is back to the anaerobic pond；
One buffer pool, for storing the waste water after the precipitation in the sedimentation basin so that the intermediate water reuse system is called.
The biochemical treatment system also includes
An at least roots blower, for leading to oxygen to the Aerobic Pond；
One first sludge treating system, is communicated in the anaerobic pond and sedimentation basin, for anaerobic pond described in circular treatment and
The precipitation of sedimentation basin, obtains waste water and sludge, and the waste water is back into the regulating reservoir.
The intermediate water reuse system includes
One more medium filter, for tentatively filtering the waste water in the buffer pool；
One ultrafiltration system, for the waste water after more medium filter filtering described in secondary filter；
One anti-wash tank, is communicated in the ultrafiltration system；
One PH regulating tanks, are communicated in the anti-wash tank；
One degassing tower, is communicated in the PH regulating tanks；
One film cleaning system, is communicated in the degassing tower；
One ion-exchanger, is communicated in the film cleaning system, obtains the preliminary purification water and regenerative wastewater；
One waste water collection tank, is communicated in the ion-exchanger, is back to for collecting regenerative wastewater, and by regenerative wastewater
The anaerobic pond.
The chemical phosphorus removal system includes
One PH initial adjustment grooves, are communicated in the ion-exchanger, and the PH initial adjustments groove is used to adjust the ion-exchanger
Preliminary purification water after processing；
One reactive tank, is communicated in the PH initial adjustments groove；
One flocculation tanks, are communicated in the reactive tank；
One stillpot, is communicated in the flocculation tanks；
One PH adjusts groove eventually, is communicated in the stillpot.
The chemical phosphorus removal system also includes
One second sludge treating system, is communicated in the stillpot and the PH initial adjustments groove, and the sludge treating system is used
In the sediment for handling the stillpot.
The utility model has the advantages that：Sewerage integrated processing system of the present utility model, it is ensured that industrial wastewater can be followed
Ring is recycled, and reduces cost, with the multicycle processing mode of multiple operation, the processing of multi-layer is carried out to waste water, makes place
Waste water after reason reaches the requirement reused of standard, and by the design of backwash, effectively raises making for system
With the utilization ratio in life-span, integrated treatment waste water reaches the effect of waste water high-efficiency processing.
Brief description of the drawings
The utility model is further explained with reference to the accompanying drawings and examples.
Fig. 1 is the sewerage integrated processing system module diagram of the utility model embodiment.
Fig. 2 is the biochemical treatment system module diagram of the utility model embodiment.
Fig. 3 is the intermediate water reuse system module diagram of the utility model embodiment.
Fig. 4 is the chemical phosphorus removal system module diagram of the utility model embodiment.
Wherein,
1 biochemical treatment system；2 intermediate water reuse systems；
3 chemical phosphorus removal systems；11 regulating reservoirs；
12 anaerobic ponds；13 anoxic ponds；
14 Aerobic Ponds；15 sedimentation basins；
16 buffer pools；17 roots blowers；
18 first sludge treating systems；21 more medium filters；
22 ultrafiltration systems；23 anti-wash tanks；
24 PH regulating tanks；25 degassing towers；
26 film cleaning systems；27 ion-exchangers；
28 waste water collection tanks；31 PH initial adjustment grooves；
32 reactive tanks；33 flocculation tanks；
34 stillpots；35 PH adjust groove eventually；
36 second sludge treating systems；4 medicine systems.
Embodiment
The explanation of following examples is the specific reality implemented to illustrate the utility model can be used to reference to additional schema
Apply example.The direction term that the utility model is previously mentioned, such as " on ", " under ", "front", "rear", "left", "right", " top ", " bottom "
Deng being only the direction with reference to annexed drawings.Therefore, the direction term used is to illustrate and understand the utility model, rather than
To limit the utility model.
Embodiment, as shown in figure 1, a kind of sewerage integrated processing system, including a biochemical treatment system 1, a reclaimed water are returned
With system 2, a chemical phosphorus removal system 3 and a medicine system 4.
As shown in Fig. 2 biochemical treatment system 1 is used to handle raw sewage for the first time in biochemical mode.Specifically, this reality
Apply in example, biochemical treatment system 1 include a regulating reservoir 11, an anaerobic pond 12, an at least anoxic pond 13, an at least Aerobic Pond 14,
One sedimentation basin 15, a buffer pool 16 and at least a roots blower 17, one first sludge treating system 18.
Regulating reservoir 11 is used for the various waste water of processing needed for adjusting distribution；Anaerobic pond 12 is used to extract in a processing pond
Waste water and remove partial organic substances in the waste water；An at least anoxic pond 13 is used to extract useless after the anaerobic pond 12 is handled
Water and remove partial organic substances in the waste water；An at least Aerobic Pond 14 is used to digest, degraded after the processing of a upper processing pond
Waste water in organic matter；Sedimentation basin 15 is used to store, precipitated after the anaerobic pond 12, anaerobic pond 12, the processing of Aerobic Pond 14
Waste water, and the waste water of precipitation is back to the anaerobic pond 12；Buffer pool 16 is heavy in the sedimentation basin 15 for storing
Waste water behind shallow lake calls for the intermediate water reuse system 2.An at least roots blower 17 is used to lead to oxygen to the Aerobic Pond 14.
Wherein, the bottom of sedimentation basin 15 connects the first sludge treating system 18, passes through muddy water of the system to sedimentation basin 15
Sediment carries out mud-water separation, obtains mud and waste water, and waste water is back into regulating reservoir 11, then does circular treatment.
Likewise, the bottom of anaerobic pond 12 connects the first sludge treating system 18, pass through mud of the system to anaerobic pond 12
Water deposit carries out mud-water separation, obtains mud and waste water, and waste water is back into regulating reservoir 11, then does circular treatment.
As shown in figure 3, intermediate water reuse system 2 is communicated in the biochemical treatment system 1, the intermediate water reuse system 2 is used for
After-treatment is carried out to the waste water after the biochemical treatment system 1 for the first time processing, regenerative wastewater and preliminary purification water is obtained, and will
Regenerative wastewater is back to the biochemical treatment system 1.In the present embodiment, the intermediate water reuse system 2 includes a multi-medium filtering
Device 21, a ultrafiltration system 22, an anti-wash tank 23, a PH regulating tanks 24, a degassing tower 25, a film cleaning system 26, an ion are handed over
Parallel operation 27, a waste water collection tank 28.
Specifically, more medium filter 21 is used to tentatively filter the waste water in the buffer pool 16.More medium filter 21
It is, using one or more of filter mediums, under pressure, to pass through certain thickness granular or non-grain material（Filtering is situated between
Matter）, so that the preliminary effective suspended impurity removed in waste water.
Ultrafiltration system 22 is used for the waste water after more medium filter 21 described in secondary filter is filtered.Anti-wash tank 23 is communicated in institute
State ultrafiltration system 22；PH regulating tanks 24 are communicated in anti-wash tank 23；Degassing tower 25 is communicated in the PH regulating tanks 24；Film cleaning system
26 are communicated in the degassing tower 25.Ion-exchanger 27 is communicated in the film cleaning system 26, obtain the preliminary purification water and
Regenerative wastewater；Waste water collection tank 28 is communicated in the ion-exchanger 27, is returned for collecting regenerative wastewater, and by regenerative wastewater
To the anaerobic pond 12.
As shown in figure 4, chemical phosphorus removal system 3 is communicated in the intermediate water reuse system 2, the chemical phosphorus removal system 3 is used for
The preliminary purification water is handled, obtains discharging water.Chemical phosphorus removal system 3 include a PH initial adjustments groove 31, a reactive tank 32,
One flocculation tanks 33, a stillpot 34, a PH adjust the sludge treating system 36 of groove 35 and 1 second eventually.
PH initial adjustments groove 31 is communicated in the ion-exchanger 27, and PH initial adjustments groove 31 is used to adjust the ion-exchanger 27
Preliminary purification water after processing.Reactive tank 32 is communicated in the PH initial adjustments groove 31；Flocculation tanks 33 are communicated in the reactive tank 32；It is heavy
Shallow lake groove 34 is communicated in the flocculation tanks 33；PH adjusts groove 35 to be communicated in the stillpot 34 eventually.Second sludge treating system 36, connection
In the stillpot 34 and the PH initial adjustments groove 31, the sludge treating system is used for the sediment for handling the stillpot 34.
Medicine system 4 is used for at the biochemical treatment system 1, intermediate water reuse system 2 and the addition of chemical phosphorus removal system 3
Manage the various reagents of waste water.
Preferred embodiment of the present utility model is these are only, it is all in this practicality not to limit the utility model
Any modifications, equivalent substitutions and improvements made within new spirit and principle etc., should be included in guarantor of the present utility model
Within the scope of shield.
Claims (6)
1. a kind of sewerage integrated processing system, it is characterised in that：Including
One biochemical treatment system, for being handled for the first time in biochemical mode raw sewage；
One intermediate water reuse system, is communicated in the biochemical treatment system, and the intermediate water reuse system is used for the biochemical treatment
Waste water after system processing for the first time carries out after-treatment, obtains regenerative wastewater and preliminary purification water, and regenerative wastewater is back to
The biochemical treatment system；
One chemical phosphorus removal system, is communicated in the intermediate water reuse system, and the chemical phosphorus removal system is used for the preliminary purification
Water is handled, and obtains discharging water；
One medicine system, for being given up for the addition processing of the biochemical treatment system, intermediate water reuse system and chemical phosphorus removal system
The various reagents of water.
2. sewerage integrated processing system according to claim 1, it is characterised in that：The biochemical treatment system includes
One regulating reservoir, the various waste water of processing needed for for adjusting distribution；
One anaerobic pond, for the waste water extracted in a upper processing pond and the partial organic substances removed in the waste water；
An at least anoxic pond, for the waste water extracted after the anaerobic pond processing and the partial organic substances removed in the waste water；
An at least Aerobic Pond, for the organic matter in the waste water after being handled through a upper processing pond that digests, degrades；
One sedimentation basin, for storing, precipitating the waste water after the anaerobic pond, anaerobic pond, Aerobic Pond processing, and by precipitation
Waste water is back to the anaerobic pond；
One buffer pool, for storing the waste water after the precipitation in the sedimentation basin so that the intermediate water reuse system is called.
3. sewerage integrated processing system according to claim 2, it is characterised in that：The biochemical treatment system also includes
An at least roots blower, for leading to oxygen to the Aerobic Pond；
One first sludge treating system, is communicated in the anaerobic pond and sedimentation basin, for anaerobic pond described in circular treatment and precipitation
The precipitation in pond, obtains waste water and sludge, and the waste water is back into the regulating reservoir.
4. sewerage integrated processing system according to claim 2, it is characterised in that：The intermediate water reuse system includes
One more medium filter, for tentatively filtering the waste water in the buffer pool；
One ultrafiltration system, for the waste water after more medium filter filtering described in secondary filter；
One anti-wash tank, is communicated in the ultrafiltration system；
One PH regulating tanks, are communicated in the anti-wash tank；
One degassing tower, is communicated in the PH regulating tanks；
One film cleaning system, is communicated in the degassing tower；
One ion-exchanger, is communicated in the film cleaning system, obtains the preliminary purification water and regenerative wastewater；
One waste water collection tank, is communicated in the ion-exchanger, for collecting regenerative wastewater, and regenerative wastewater is back to described
Anaerobic pond.
5. sewerage integrated processing system according to claim 4, it is characterised in that：The chemical phosphorus removal system includes
One PH initial adjustment grooves, are communicated in the ion-exchanger, and the PH initial adjustments groove is used for the processing for adjusting the ion-exchanger
Preliminary purification water afterwards；
One reactive tank, is communicated in the PH initial adjustments groove；
One flocculation tanks, are communicated in the reactive tank；
One stillpot, is communicated in the flocculation tanks；
One PH adjusts groove eventually, is communicated in the stillpot.
6. sewerage integrated processing system according to claim 5, it is characterised in that：The chemical phosphorus removal system also includes
One second sludge treating system, is communicated in the stillpot and the PH initial adjustments groove, and the sludge treating system is used to locate
Manage the sediment of the stillpot.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720097619.8U CN206447735U (en) | 2017-01-25 | 2017-01-25 | A kind of sewerage integrated processing system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720097619.8U CN206447735U (en) | 2017-01-25 | 2017-01-25 | A kind of sewerage integrated processing system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206447735U true CN206447735U (en) | 2017-08-29 |
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ID=59668008
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201720097619.8U Expired - Fee Related CN206447735U (en) | 2017-01-25 | 2017-01-25 | A kind of sewerage integrated processing system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN206447735U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108862750A (en) * | 2018-06-26 | 2018-11-23 | 苏州他山石环保科技有限公司 | A kind of Nitrogen-and Phosphorus-containing sewage disposal device and intermediate water reuse system and its method |
-
2017
- 2017-01-25 CN CN201720097619.8U patent/CN206447735U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108862750A (en) * | 2018-06-26 | 2018-11-23 | 苏州他山石环保科技有限公司 | A kind of Nitrogen-and Phosphorus-containing sewage disposal device and intermediate water reuse system and its method |
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| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20170829 Termination date: 20200125 |
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| CF01 | Termination of patent right due to non-payment of annual fee |