CN204138457U - A kind of high COD, multiple types waste emulsified mixture breaking device - Google Patents
A kind of high COD, multiple types waste emulsified mixture breaking device Download PDFInfo
- Publication number
- CN204138457U CN204138457U CN201420057485.3U CN201420057485U CN204138457U CN 204138457 U CN204138457 U CN 204138457U CN 201420057485 U CN201420057485 U CN 201420057485U CN 204138457 U CN204138457 U CN 204138457U
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- China
- Prior art keywords
- heat exchanger
- multiple types
- breaking device
- filter press
- frame filter
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Abstract
The utility model discloses a kind of high COD, multiple types waste emulsified mixture breaking device, comprise heat exchanger, and the reactor be connected successively with heat exchanger, No. 1 equalizing tank, plate-and-frame filter press; Described plate-and-frame filter press is also connected with sludge sump; Described plate-and-frame filter press is also connected with heat exchanger; Described inside reactor is disposed with acidifying setting device, FeSO4 breaking device, limestone vegetation device and flocculation reaction device; Because the utility model can realize focusing on multiple emulsifying liquid waste water, reduce the intractability of emulsifying liquid waste water to a great extent, effectively ensure that the demulsification of the emulsion of high density, multiple types, and can ensure that water outlet reaches the requirement of subsequent biochemical process, reduce the labour intensity of staff simultaneously, improve the economic benefit of enterprise.
Description
Technical field
The utility model relates to a kind of high COD, multiple types waste emulsified mixture breaking device.
Background technology
Emulsifying liquid waste water is waste water common in plant produced, is characterized in various in style, COD
crhigh with oleaginousness concentration, intractability is large; Waste emulsified mixture treatment technology conventional at present has heating method, salting-out process, coacervation, acidization etc., and these methods are only applicable to process a certain waste emulsified mixture; But in actual process, the kind often comprising emulsion is more, and complicated component, such as: emulsifying liquid waste water, electroplating wastewater, percolate etc., use single method cannot realize focusing on, and the effect of desirable breakdown of emulsion and degraded COD cannot be reached.
Summary of the invention
The technical problems to be solved in the utility model is to provide one and can realizes focusing on emulsion, and reaches high COD, the multiple types waste emulsified mixture breaking device of breakdown of emulsion and degraded COD.
For solving the problem, the utility model adopts following technical scheme:
High COD of the present utility model, multiple types waste emulsified mixture breaking device, comprise heat exchanger, and the reactor be connected successively with heat exchanger, No. 1 equalizing tank, plate-and-frame filter press; Described plate-and-frame filter press is also connected with sludge sump; Described plate-and-frame filter press is also connected with heat exchanger; Described inside reactor is disposed with acidifying setting device, FeSO4 breaking device, limestone vegetation device and flocculation reaction device.
Further, described reactor is also connected with water pump by heat exchanger.
Further, described internal heat exchanger is provided with heating unit.
Further, described acidifying setting device inside is also provided with chemicals dosing plant.
Further, described plate-and-frame filter press inside is also provided with spiral pump.
Compared with prior art, it has following beneficial effect to the utility model: one of the present utility model can realize focusing on emulsion, and reaches high COD, the multiple types waste emulsified mixture breaking device of breakdown of emulsion and degraded COD; Because the utility model can realize focusing on multiple emulsifying liquid waste water, reduce the intractability of emulsifying liquid waste water to a great extent, effectively ensure that the demulsification of the emulsion of high density, multiple types, and can ensure that water outlet reaches the requirement of subsequent biochemical process, reduce the labour intensity of staff simultaneously, improve the economic benefit of enterprise.
Accompanying drawing explanation
Fig. 1 is structured flowchart of the present utility model.
1-heat exchanger; 2-reactor; 3-1 equalizing tank; 4-plate-and-frame filter press; 5-sludge sump; 6-acidifying setting device; 7-FeSO4 breaking device; 8-limestone vegetation device; 9-flocculation reaction device; 10-water pump; 11-heating unit.
Embodiment
The high COD of one as shown in Figure 1, multiple types waste emulsified mixture breaking device, comprise heat exchanger 1, and reactor 2, No. 1 equalizing tank 3, plate-and-frame filter press 4 of being connected successively with heat exchanger; Described plate-and-frame filter press 4 is also connected with sludge sump 5; Described plate-and-frame filter press 4 is also connected with heat exchanger 1; Described reactor 2 inside is disposed with acidifying setting device 6, FeSO4 breaking device 7, limestone vegetation device 8 and flocculation reaction device 9.
Wherein, described reactor 2 is also connected with water pump 10 by heat exchanger 1; Described heat exchanger 1 inside is provided with heating unit 11; Described acidifying setting device 6 inside is also provided with chemicals dosing plant; Described plate-and-frame filter press 4 inside is also provided with spiral pump.
One of the present utility model can realize focusing on emulsion, and reaches high COD, the multiple types waste emulsified mixture breaking device of breakdown of emulsion and degraded COD; Because the utility model can realize focusing on multiple emulsifying liquid waste water, reduce the intractability of emulsifying liquid waste water to a great extent, effectively ensure that the demulsification of the emulsion of high density, multiple types, and can ensure that water outlet reaches the requirement of subsequent biochemical process, reduce the labour intensity of staff simultaneously, improve the economic benefit of enterprise.
The above, be only embodiment of the present utility model, but protection domain of the present utility model is not limited thereto, and any change of expecting without creative work or replacement, all should be encompassed within protection domain of the present utility model.Therefore, the protection domain that protection domain of the present utility model should limit with claims is as the criterion.
Claims (5)
1. high COD, a multiple types waste emulsified mixture breaking device, is characterized in that: comprise heat exchanger, and the reactor be connected successively with heat exchanger, No. 1 equalizing tank, plate-and-frame filter press; Described plate-and-frame filter press is also connected with sludge sump; Described plate-and-frame filter press is also connected with heat exchanger; Described inside reactor is disposed with acidifying setting device, FeSO4 breaking device, limestone vegetation device and flocculation reaction device.
2. high COD according to claim 1, multiple types waste emulsified mixture breaking device, is characterized in that: described reactor is also connected with water pump by heat exchanger.
3. high COD according to claim 1, multiple types waste emulsified mixture breaking device, is characterized in that: described internal heat exchanger is provided with heating unit.
4. high COD according to claim 1, multiple types waste emulsified mixture breaking device, is characterized in that: described acidifying setting device inside is also provided with chemicals dosing plant.
5. high COD according to claim 1, multiple types waste emulsified mixture breaking device, is characterized in that: described plate-and-frame filter press inside is also provided with spiral pump.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420057485.3U CN204138457U (en) | 2014-01-28 | 2014-01-28 | A kind of high COD, multiple types waste emulsified mixture breaking device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420057485.3U CN204138457U (en) | 2014-01-28 | 2014-01-28 | A kind of high COD, multiple types waste emulsified mixture breaking device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN204138457U true CN204138457U (en) | 2015-02-04 |
Family
ID=52415159
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201420057485.3U Expired - Fee Related CN204138457U (en) | 2014-01-28 | 2014-01-28 | A kind of high COD, multiple types waste emulsified mixture breaking device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN204138457U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103896428A (en) * | 2014-01-28 | 2014-07-02 | 青岛新天地固体废物综合处置有限公司 | High-COD (chemical oxygen demand) and multi-variety waste emulsion breaking device and breaking method |
| CN106977035A (en) * | 2017-05-24 | 2017-07-25 | 广西碧清源环保科技有限公司 | A kind of processing for mixing waste emulsified mixture, retracting device |
-
2014
- 2014-01-28 CN CN201420057485.3U patent/CN204138457U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103896428A (en) * | 2014-01-28 | 2014-07-02 | 青岛新天地固体废物综合处置有限公司 | High-COD (chemical oxygen demand) and multi-variety waste emulsion breaking device and breaking method |
| CN106977035A (en) * | 2017-05-24 | 2017-07-25 | 广西碧清源环保科技有限公司 | A kind of processing for mixing waste emulsified mixture, retracting device |
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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: 20150204 Termination date: 20170128 |