CN204958664U - Processing system of medicine waste water - Google Patents
Processing system of medicine waste water Download PDFInfo
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- CN204958664U CN204958664U CN201520645766.5U CN201520645766U CN204958664U CN 204958664 U CN204958664 U CN 204958664U CN 201520645766 U CN201520645766 U CN 201520645766U CN 204958664 U CN204958664 U CN 204958664U
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- waste water
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- treatment system
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Abstract
The utility model discloses a processing system of medicine waste water, including oil interceptor, triple -effect evaporator, bio -contact oxidation tank, SBR pond, two heavy pond, coagulating basin and the denitrification filtering ponds that connect gradually. The utility model discloses an oil slick is kept apart to the oil interceptor, adopts triple -effect evaporator to get rid of sodium chloride and partial organic matter, adopts biodegradable, SBR technology and two sinks and further get rid of the organic matter in the waste water, and effect through coagulating basin and denitrification filtering pond further reduces CODcr and BOD5, can guarantee stably moreover that SS, TP are up to standard. The utility model discloses an overall structure is simple, and it is convenient to implement, and it is up to standard to go out water stabilization of water quality.
Description
Technical field
The utility model relates to technical field of waste water processing, specifically a kind for the treatment of system of pharmaceutical wastewater.
Background technology
Since 20th century, developing rapidly of medicine industry, brings leap to human civilization, and meanwhile, the pollution of the waste water emitted in its production process to environment also increasingly sharpens, and brings serious threat to human health.It is reported, pharmaceutical wastewater complicated component, concentration and salinity are high, colourity and toxicity is large, often containing miscellaneous organic pollution materials, have the material much belonging to bio-refractory in these materials, can retain in environment within considerable time.Particularly to human health risk greatly " three cause " (carcinogenic, teratogenesis, mutagenesis) organic pollutant, even if concentration, lower than still can the human health of serious harm during 10-9 level, adopts traditional treatment process to be difficult to qualified discharge in water body.
Utility model content
The technical problems to be solved in the utility model is to provide a kind for the treatment of system of pharmaceutical wastewater, and the waste water after its process meets national emission request, and reusable edible.
The technical solution of the utility model is:
A kind for the treatment of system of pharmaceutical wastewater, include connect successively oil trap, triple-effect evaporator, biological contact oxidation pond, SBR pond, second pond, coagulation basin and denitrification filter pool, wherein, the gas after the evaporation of triple-effect evaporator enters biological contact oxidation pond after condenser condenses.
Waste water after described condenser condenses enters biological contact oxidation pond after being introduced into pH value equalizing tank.
The front end of described oil trap is connected with artificial grid.
Described denitrification filter pool and carbon source are speculated pump and are connected.
The sludge outlet rear end of described second pond is connected with sludge thickener and chamber filter press in turn.
Advantage of the present utility model:
The utility model adopts oil trap isolation oil slick, triple-effect evaporator is adopted to remove sodium-chlor and partial organic substances, adopt biological degradation, SBR technique and the two heavy organism removed further in waste water, by the effect of coagulation basin and denitrification filter pool, further reduction CODcr and BOD5, and it is up to standard to stablize guarantee SS, TP.One-piece construction of the present utility model is simple, and it is convenient to implement, and stable effluent quality is up to standard.
Accompanying drawing explanation
Fig. 1 is structural representation of the present utility model.
Embodiment
A kind for the treatment of system of pharmaceutical wastewater, include connect successively artificial grid 1, oil trap 2, triple-effect evaporator 3, pH value equalizing tank 4, biological contact oxidation pond 5, SBR pond 6, second pond 7, coagulation basin 8 and denitrification filter pool 9, wherein, gas after the evaporation of triple-effect evaporator 3 enters pH value equalizing tank 4 after condenser condenses, denitrification filter pool 9 and carbon source are speculated pump 10 and are connected, carbon source is speculated pump 10 timing and add carbon source in denitrification filter pool 9, and the sludge outlet rear end of second pond 7 is connected with sludge thickener 11 and chamber filter press 12 in turn.
Claims (5)
1. the treatment system of a pharmaceutical wastewater, it is characterized in that: include connect successively oil trap, triple-effect evaporator, biological contact oxidation pond, SBR pond, second pond, coagulation basin and denitrification filter pool, wherein, the gas after the evaporation of triple-effect evaporator enters biological contact oxidation pond after condenser condenses.
2. the treatment system of a kind of pharmaceutical wastewater according to claim 1, is characterized in that: the waste water after described condenser condenses enters biological contact oxidation pond after being introduced into pH value equalizing tank.
3. the treatment system of a kind of pharmaceutical wastewater according to claim 1, is characterized in that: the front end of described oil trap is connected with artificial grid.
4. the treatment system of a kind of pharmaceutical wastewater according to claim 1, is characterized in that: described denitrification filter pool and carbon source are speculated pump and be connected.
5. the treatment system of a kind of pharmaceutical wastewater according to claim 1, is characterized in that: the sludge outlet rear end of described second pond is connected with sludge thickener and chamber filter press in turn.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520645766.5U CN204958664U (en) | 2015-08-26 | 2015-08-26 | Processing system of medicine waste water |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520645766.5U CN204958664U (en) | 2015-08-26 | 2015-08-26 | Processing system of medicine waste water |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN204958664U true CN204958664U (en) | 2016-01-13 |
Family
ID=55053744
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201520645766.5U Expired - Fee Related CN204958664U (en) | 2015-08-26 | 2015-08-26 | Processing system of medicine waste water |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN204958664U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107226579A (en) * | 2016-03-24 | 2017-10-03 | 福建省三净环保科技有限公司 | A kind of sewage disposal device |
| CN112010497A (en) * | 2020-07-23 | 2020-12-01 | 九江博泰环保有限公司 | High ammonia nitrogen wastewater treatment process |
-
2015
- 2015-08-26 CN CN201520645766.5U patent/CN204958664U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107226579A (en) * | 2016-03-24 | 2017-10-03 | 福建省三净环保科技有限公司 | A kind of sewage disposal device |
| CN112010497A (en) * | 2020-07-23 | 2020-12-01 | 九江博泰环保有限公司 | High ammonia nitrogen wastewater treatment process |
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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 | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20160113 Termination date: 20210826 |