CN203781881U - Electrolysis flocculation reaction device - Google Patents
Electrolysis flocculation reaction device Download PDFInfo
- Publication number
- CN203781881U CN203781881U CN201420178833.2U CN201420178833U CN203781881U CN 203781881 U CN203781881 U CN 203781881U CN 201420178833 U CN201420178833 U CN 201420178833U CN 203781881 U CN203781881 U CN 203781881U
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- pipeline
- power supply
- tank
- reactive tank
- flocculation reaction
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Abstract
The utility model discloses an electrolysis flocculation reaction device which comprises a reaction tank, a high-level water tank, a filter and a direct-current voltage stabilizing power supply, wherein the reaction tank is internally provided with a metal electrode plate; a plurality of graphite electrode masts are arranged at the lower end of the metal electrode plate; the anode of the direct-current voltage stabilizing power supply is connected with the metal electrode plate; the cathode of the direct-current voltage stabilizing power supply is connected with the graphite electrode masts; the high-level water tank is connected with a gauge through a pipeline; the gauge is connected to the left side of the reaction tank through another pipeline; a water pump is connected to the right side of the reaction tank through another pipeline; the water tank is connected to the upper end of a filter through another pipeline; a water outlet tube is arranged at the lower end of the filter; a dross discharge ditch is formed in the upper end of the reaction tank. The device has the advantages of simple equipment, good impact resistance, convenience in operation and freedom of chemical reagents.
Description
Technical field
The utility model relates to a kind of electrolytic flocculation reaction unit, belongs to water treatment field.
Background technology
At present, wait in manufacturing enterprise some resins are synthetic, can produce a large amount of organic high-salinity wastewater, current also comparatively original for the processing means of organic high-salinity wastewater, and use chemical agent easily to cause secondary pollution, make waste water be difficult to reach emission standard.
Utility model content
Technical problem to be solved in the utility model is to provide that a kind of equipment is simple, shock-resistance good, easy to operate, do not need to add chemical agent electrolytic flocculation reaction unit.
In order to solve the problems of the technologies described above, the technical solution adopted in the utility model is: a kind of electrolytic flocculation reaction unit, comprise reactive tank, elevated tank, strainer and D.C. regulated power supply, in described reactive tank, be provided with metal electrode board, described metal electrode board lower end is provided with some graphite electrode columns, the anodal connection metal battery lead plate of described D.C. regulated power supply, described D.C. regulated power supply negative pole connects graphite electrode columns, described elevated tank connects gauger by pipeline, described gauger is by pipeline ligation groove left side, described reactive tank right side is connected with water pump by pipeline, described water pump connects strainer upper end by pipeline, described strainer lower end is provided with rising pipe, described reactive tank upper end is provided with scum silica frost and goes out slag runner.
In described elevated tank, be provided with whipping appts.
Described reactive tank lower end is provided with drainage for overhaul pipe.
The utlity model has following advantage:
A, do not need to add chemical agent, can save medicament and administration apparatus expense;
B, processing costs are low, and equipment is simple, easily realizes automatic management;
C, device operability are strong, and in the time that water quality and quantity changes, adjustable current density, makes water outlet reach processing requirements.
Brief description of the drawings
Fig. 1 is the utility model structural representation.
In figure: 1, reactive tank; 2, elevated tank; 3, strainer; 4, D.C. regulated power supply; 5, graphite electrode columns; 6, D.C. regulated power supply; 7, gauger; 8, water pump; 9, rising pipe; 10, scum silica frost goes out slag runner; 11, whipping appts; 12, drainage for overhaul pipe.
Embodiment
Below in conjunction with accompanying drawing, and, the utility model is described further in conjunction with the embodiments.
As shown in Figure 1, a kind of electrolytic flocculation reaction unit of the present embodiment, comprise reactive tank 1, elevated tank 2, strainer 3 and D.C. regulated power supply 6, in described reactive tank 1, be provided with metal electrode board 4, described metal electrode board 4 lower ends are provided with some graphite electrode columns 5, the anodal connection metal battery lead plate 4 of described D.C. regulated power supply 6, described D.C. regulated power supply 6 negative poles connect graphite electrode columns 5, described elevated tank 2 connects gauger 7 by pipeline, described gauger 7 is by pipeline ligation groove 1 left side, described reactive tank 1 right side is connected with water pump 8 by pipeline, described water pump 8 connects strainer 3 upper ends by pipeline, described strainer 3 lower ends are provided with rising pipe 9, described reactive tank 1 upper end is provided with scum silica frost and goes out slag runner 10.
In described elevated tank 2, be provided with whipping appts 11.
Described reactive tank 1 lower end is provided with drainage for overhaul pipe 12.
The solidifying wadding method of electrolysis is processed organic high-salinity wastewater, and in the time of electrolysis, organism is polarized, and charged organism part is participated in reaction, is degraded; The solidifying wadding reaction forming when electrolysis simultaneously, the wadding forming flower, the comprehensive actions such as absorption, bridge formation and the electrical neutralization of generation, are purified waste water.
The utility model, compared with traditional product, the utlity model has following advantage: do not need to add chemical agent, can save medicament and administration apparatus expense; Processing costs is low, and equipment is simple, easily realizes automatic management; Device operability is strong, and in the time that water quality and quantity changes, adjustable current density, makes water outlet reach processing requirements.
Claims (3)
1. an electrolytic flocculation reaction unit, it is characterized in that: comprise reactive tank (1), elevated tank (2), strainer (3) and D.C. regulated power supply (6), in described reactive tank (1), be provided with metal electrode board (4), described metal electrode board (4) lower end is provided with some graphite electrode columns (5), the described anodal connection metal battery lead plate of D.C. regulated power supply (6) (4), described D.C. regulated power supply (6) negative pole connects graphite electrode columns (5), described elevated tank (2) connects gauger (7) by pipeline, described gauger (7) is by pipeline ligation groove (1) left side, described reactive tank (1) right side is connected with water pump (8) by pipeline, described water pump (8) connects strainer (3) upper end by pipeline, described strainer (3) lower end is provided with rising pipe (9), described reactive tank (1) upper end is provided with scum silica frost and goes out slag runner (10).
2. a kind of electrolytic flocculation reaction unit according to claim 1, is characterized in that: in described elevated tank (2), be provided with whipping appts (11).
3. a kind of electrolytic flocculation reaction unit according to claim 1, is characterized in that: described reactive tank (1) lower end is provided with drainage for overhaul pipe (12).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420178833.2U CN203781881U (en) | 2014-04-14 | 2014-04-14 | Electrolysis flocculation reaction device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420178833.2U CN203781881U (en) | 2014-04-14 | 2014-04-14 | Electrolysis flocculation reaction device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN203781881U true CN203781881U (en) | 2014-08-20 |
Family
ID=51318089
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201420178833.2U Expired - Fee Related CN203781881U (en) | 2014-04-14 | 2014-04-14 | Electrolysis flocculation reaction device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN203781881U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105585082A (en) * | 2015-12-24 | 2016-05-18 | 哈尔滨工业大学水资源国家工程研究中心有限公司 | Integrated electrochemical treatment device for deep treatment and deep treatment method |
-
2014
- 2014-04-14 CN CN201420178833.2U patent/CN203781881U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105585082A (en) * | 2015-12-24 | 2016-05-18 | 哈尔滨工业大学水资源国家工程研究中心有限公司 | Integrated electrochemical treatment device for deep treatment and deep treatment method |
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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: 20140820 Termination date: 20170414 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |