CN202016919U - Garbage sewage treatment device - Google Patents
Garbage sewage treatment device Download PDFInfo
- Publication number
- CN202016919U CN202016919U CN2011201498162U CN201120149816U CN202016919U CN 202016919 U CN202016919 U CN 202016919U CN 2011201498162 U CN2011201498162 U CN 2011201498162U CN 201120149816 U CN201120149816 U CN 201120149816U CN 202016919 U CN202016919 U CN 202016919U
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- Prior art keywords
- communicated
- outlet
- pond
- electrolysis pond
- inlet
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
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- 239000010865 sewage Substances 0.000 title claims abstract description 34
- 239000010813 municipal solid waste Substances 0.000 title claims abstract description 26
- 238000005868 electrolysis reaction Methods 0.000 claims description 40
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 19
- CBENFWSGALASAD-UHFFFAOYSA-N Ozone Chemical compound [O-][O+]=O CBENFWSGALASAD-UHFFFAOYSA-N 0.000 claims description 12
- 238000000746 purification Methods 0.000 claims description 10
- 239000002893 slag Substances 0.000 claims description 10
- 238000006243 chemical reaction Methods 0.000 claims description 3
- 230000000694 effects Effects 0.000 abstract description 7
- 238000000034 method Methods 0.000 description 13
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 6
- 239000000126 substance Substances 0.000 description 6
- XKMRRTOUMJRJIA-UHFFFAOYSA-N ammonia nh3 Chemical compound N.N XKMRRTOUMJRJIA-UHFFFAOYSA-N 0.000 description 5
- 229910052742 iron Inorganic materials 0.000 description 5
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 4
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 4
- 238000001311 chemical methods and process Methods 0.000 description 4
- 239000001257 hydrogen Substances 0.000 description 4
- 229910052739 hydrogen Inorganic materials 0.000 description 4
- -1 iron ion Chemical class 0.000 description 4
- 239000001301 oxygen Substances 0.000 description 4
- 229910052760 oxygen Inorganic materials 0.000 description 4
- 238000011026 diafiltration Methods 0.000 description 3
- 238000001914 filtration Methods 0.000 description 3
- 238000005516 engineering process Methods 0.000 description 2
- 239000012535 impurity Substances 0.000 description 2
- 238000007254 oxidation reaction Methods 0.000 description 2
- 239000000243 solution Substances 0.000 description 2
- 239000002351 wastewater Substances 0.000 description 2
- 230000003245 working effect Effects 0.000 description 2
- PWHULOQIROXLJO-UHFFFAOYSA-N Manganese Chemical compound [Mn] PWHULOQIROXLJO-UHFFFAOYSA-N 0.000 description 1
- 238000010521 absorption reaction Methods 0.000 description 1
- 239000012267 brine Substances 0.000 description 1
- 239000003610 charcoal Substances 0.000 description 1
- 230000002950 deficient Effects 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 239000010419 fine particle Substances 0.000 description 1
- 238000005189 flocculation Methods 0.000 description 1
- 230000016615 flocculation Effects 0.000 description 1
- 238000003973 irrigation Methods 0.000 description 1
- 230000002262 irrigation Effects 0.000 description 1
- 229910052748 manganese Inorganic materials 0.000 description 1
- 239000011572 manganese Substances 0.000 description 1
- 239000012528 membrane Substances 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 150000002739 metals Chemical class 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 239000013049 sediment Substances 0.000 description 1
- 230000011218 segmentation Effects 0.000 description 1
- 239000010801 sewage sludge Substances 0.000 description 1
- 239000010802 sludge Substances 0.000 description 1
- HPALAKNZSZLMCH-UHFFFAOYSA-M sodium;chloride;hydrate Chemical compound O.[Na+].[Cl-] HPALAKNZSZLMCH-UHFFFAOYSA-M 0.000 description 1
- 239000002689 soil Substances 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 230000006641 stabilisation Effects 0.000 description 1
- 238000011105 stabilization Methods 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
Landscapes
- Water Treatment By Electricity Or Magnetism (AREA)
- Treatment Of Water By Oxidation Or Reduction (AREA)
Abstract
The utility model discloses a garbage sewage treatment device, which belongs to the technical field of sewage treatment devices and comprises a sewage pool, wherein an outlet of the sewage pool is communicated with an inlet of a primary filter, an outlet of the primary filter is communicated with an inlet of a secondary filter, and a pulse electrolytic cell is connected between the primary filter and the secondary filter, wherein the outlet of the primary filter is communicated with an inlet of the pulse electrolytic cell, an outlet of the pulse electrolytic cell is communicated with the inlet of the secondary filter, and the pulse electrolytic cell is connected with a pulse generator. The garbage sewage treatment device has the advantages that the sewage treatment cost is low, the operation is simple, and the treatment effect is good. The garbage sewage treatment device is mainly applicable to domestic garbage sewage treatment.
Description
Technical field
The utility model relates to a kind of waste disposal plant, especially relates to a kind of garbage leachate treatment unit.
Background technology
The effusion or the diafiltration sewage of rubbish squeezing all are high concentrated organic wastewaters of complicated component, and the smell is awful, and the inconvenience transportation, therefore are the problem demanding prompt solutions in the sewage disposal.At present the effusion of rubbish squeezing or the treatment process commonly used of diafiltration sewage there are aerobic treatment, anaerobic biological treatment, physico-chemical process and land law four big classes.One, aerobic treatment, aerobic treatment can reduce BOD5, COD and ammonia nitrogen effectively, can also remove other pollution substances such as metals such as iron, manganese.Handle percolate with aerobic methods such as activated sludge process, oxidation ditch, aerobic stabilization pond, blodiscs successful experience is all arranged.Two, anaerobic biological treatment, in recent years, the anaerobic biological treatment method of exploitation has: anaerobic biofilter, anaerobism contact tank, upflow type anaerobic sewage sludge reactor and segmentation anaerobism are nitrated etc.Three, physico-chemical process, physico-chemical process are one of methods the most frequently used in the percolate aftertreatment technology, comprise flocculation sediment, charcoal absorption, membrane sepn and chemical oxidization method etc.But the physico-chemical process processing cost is higher, is unsuitable for the processing of a large amount of percolates.Four, land law.That is the soil irrigation method, be the human sewage treatment that adopts the earliest, floor space is bigger, is used for city domestic sewage more and handles.Though above-mentioned sewage disposal way can be carried out sewage disposal, all has certain defective, such as the cost height that has, have just be fit to a small amount of sewage disposal, the occupation of land that has is wide.
The utility model content
The utility model provides a kind of garbage leachate treatment unit that a kind of garbage leachate processing cost is low, simple to operate, treatment effect is good.
The technical solution of the utility model is: a kind of garbage leachate treatment unit, comprise sewage lagoon, the outlet of described sewage lagoon is communicated with the inlet of prime filter, the outlet of prime filter is communicated with the inlet of secondary filter, be connected with the pulse electrolysis pond between described prime filter and the described secondary filter, wherein, the outlet of described prime filter is communicated with the inlet in pulse electrolysis pond, the outlet in described pulse electrolysis pond is communicated with the inlet of secondary filter, and described pulse electrolysis pond is connected with surge generator.
High-frequency impulse electrolysis pond is adopted in described pulse electrolysis pond, and described high-frequency impulse electrolysis pond is connected with high frequency pulse generator.Also can select low-frequency pulse electrolysis pond as required.Utilize concentrated high-energy in high-frequency impulse electrolysis pond and suitable frequency, organism in the garbage leachate and ammonia nitrogen thing molecular grouping are pulverized, iron ion chemical combination with the electrode generation, form new molecular grouping, held up by the bubble of the hydrogen of yin, yang electrolysis water generates and oxygen and to emerge and collect, sewage is handled completely.
Be connected with the reversing controller that makes the conversion of high frequency pulse generator positive and negative electrode between described high-frequency impulse electrolysis pond and the high frequency pulse generator.The effect of reversing controller is can be so that work-ing life of pole plate in the pulse electrolysis pond.
Described pulse electrolysis pond is connected with slag trap, and wherein, high-frequency impulse electrolysis pond can be adopted in the pulse electrolysis pond.The effect of slag trap is that these emersion things are collected by slag trap, prevent secondary pollution because the sewage surface of handling in the high-frequency electrolysis pond has a large amount of emersion things.
The outlet of described secondary filter is communicated with the ozone purification pond.Enter in the treating pond by the filtering treating water of secondary filter, the treating water for the treatment of pond is charged into ozone, it is fully purified treating water.
The outlet in described ozone purification pond is communicated with clean water basin.The water that comes out in the ozone purification pond is connected to clean water basin, can utilize once more.
Sewage disposal principle of the present utility model: the effusion or the diafiltration sewage of rubbish squeezing enter sewage lagoon, and the impurity in the sewage sinks to by self gravitation at the bottom of the pond, and afterwards, sewage enters prime filter, and prime filter is removed the sewage by suspended particle; Afterwards, sewage enters the pulse electrolysis pond, high-energy and appropriate frequency by the pulse electrolysis pond, organism in the garbage leachate and ammonia nitrogen thing molecular grouping are pulverized, iron ion chemical combination with the electrode generation, form new molecular grouping, held up by the bubble of the hydrogen of yin, yang electrolysis water generates and oxygen and emerge and collect by slag trap; Then, waste water enters secondary filter, further filtering fine-particle solid of secondary filter and impurity; At last, treating water enters the ozone purification pond, enters clean water basin reuse or discharging through the water that charges into after ozone purification is handled.
Technique effect of the present utility model: compare with existing garbage leachate treatment facility, the utility model technical process is short, and apparatus structure is greatly simplified, processing cost is low, and can handle at any time, not have the purchase and the storage problem of oxygenant, also not exist and take up an area of wide problem; The utility model pulse electrolysis pond utilizes its high-energy and appropriate frequency, organism in the garbage leachate and ammonia nitrogen thing molecular grouping are pulverized, iron ion chemical combination with the electrode generation, form new molecular grouping, held up by the bubble of the hydrogen of yin, yang electrolysis water generates and oxygen and emerge and collect by slag trap.
Description of drawings
The utility model will illustrate by example and with reference to the mode of accompanying drawing, wherein:
Fig. 1 is the structured flowchart of the utility model preferred implementation.
Embodiment
Disclosed all features in this specification sheets, or the step in disclosed all methods or the process except mutually exclusive feature and/or step, all can make up by any way.
Disclosed arbitrary feature in this specification sheets (comprising any accessory claim, summary and accompanying drawing) is unless special narration all can be replaced by other equivalences or the alternative features with similar purpose.That is, unless special narration, each feature is an example in a series of equivalences or the similar characteristics.
Present embodiment is a preferred implementation of the present utility model.
As shown in Figure 1, a kind of garbage leachate treatment unit, comprise sewage lagoon, the outlet of described sewage lagoon is communicated with the inlet of prime filter, the outlet of prime filter is communicated with the inlet in high-frequency impulse electrolysis pond, the outlet in described high-frequency impulse electrolysis pond is communicated with the inlet of secondary filter, described high-frequency impulse electrolysis pond is connected with high frequency pulse generator, wherein, high-frequency impulse electrolysis pond utilizes its high-energy of concentrating and suitable frequency, organism in the garbage leachate and ammonia nitrogen thing molecular grouping are pulverized, iron ion chemical combination with the electrode generation, form new molecular grouping, by cloudy, hydrogen that the positive electrode brine electrolysis produces and the picking-up of the bubble of oxygen emerge and collect, and sewage is handled completely.Described high-frequency impulse electrolysis pond is connected with slag trap, and the effect of slag trap is that these emersion things are collected by slag trap, prevent secondary pollution because the sewage surface of handling in the high-frequency electrolysis pond has a large amount of emersion things.
Be connected with the reversing controller that makes the conversion of high frequency pulse generator positive and negative electrode between described high-frequency impulse electrolysis pond and the high frequency pulse generator.The effect of reversing controller is can be so that work-ing life of pole plate in the pulse electrolysis pond.
The outlet of described secondary filter is communicated with the inlet in ozone purification pond.Enter in the treating pond by the filtering treating water of secondary filter, the treating water for the treatment of pond is charged into ozone, it is fully purified treating water.
The outlet in described ozone purification pond is communicated with clean water basin.The water that comes out in the ozone purification pond is connected to clean water basin, can utilize once more.
The utility model is not limited to aforesaid embodiment.The utility model expands to any new feature or any new combination that discloses in this manual, and the arbitrary new method that discloses or step or any new combination of process.
Claims (7)
1. garbage leachate treatment unit, comprise sewage lagoon, the outlet of described sewage lagoon is communicated with the inlet of prime filter, the outlet of prime filter is communicated with the inlet of secondary filter, it is characterized in that, is connected with the pulse electrolysis pond between described prime filter and the described secondary filter, wherein, the outlet of described prime filter is communicated with the inlet in pulse electrolysis pond, and the outlet in described pulse electrolysis pond is communicated with the inlet of secondary filter, and described pulse electrolysis pond is connected with surge generator.
2. garbage leachate treatment unit according to claim 1 is characterized in that, high-frequency impulse electrolysis pond is adopted in described pulse electrolysis pond, and described high-frequency impulse electrolysis pond is connected with high frequency pulse generator.
3. garbage leachate treatment unit according to claim 2 is characterized in that, is connected with the reversing controller that makes the conversion of high frequency pulse generator positive and negative electrode between described high-frequency impulse electrolysis pond and the high frequency pulse generator.
4. garbage leachate treatment unit according to claim 1 is characterized in that, described pulse electrolysis pond is connected with slag trap.
5. garbage leachate treatment unit according to claim 2 is characterized in that, described high-frequency impulse electrolysis pond is connected with slag trap.
6. according to any described garbage leachate treatment unit of claim 1 to 5, it is characterized in that the outlet of described secondary filter is communicated with the ozone purification pond.
7. garbage leachate treatment unit according to claim 6 is characterized in that, the outlet in described ozone purification pond is communicated with clean water basin.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011201498162U CN202016919U (en) | 2011-05-12 | 2011-05-12 | Garbage sewage treatment device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011201498162U CN202016919U (en) | 2011-05-12 | 2011-05-12 | Garbage sewage treatment device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN202016919U true CN202016919U (en) | 2011-10-26 |
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ID=44810593
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2011201498162U Expired - Fee Related CN202016919U (en) | 2011-05-12 | 2011-05-12 | Garbage sewage treatment device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN202016919U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107840441A (en) * | 2017-11-30 | 2018-03-27 | 河海大学 | Intelligent suitching type ozone/electric filter collaboration water treatment facilities and the method using its progress water process |
| CN111762929A (en) * | 2020-06-24 | 2020-10-13 | 河南工学院 | A landfill permeate treatment method based on electrochemical oxidation technology |
-
2011
- 2011-05-12 CN CN2011201498162U patent/CN202016919U/en not_active Expired - Fee Related
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107840441A (en) * | 2017-11-30 | 2018-03-27 | 河海大学 | Intelligent suitching type ozone/electric filter collaboration water treatment facilities and the method using its progress water process |
| CN107840441B (en) * | 2017-11-30 | 2021-01-05 | 河海大学 | Intelligent switching type ozone/electric filtration synergistic water treatment equipment and method for performing water treatment by using same |
| CN111762929A (en) * | 2020-06-24 | 2020-10-13 | 河南工学院 | A landfill permeate treatment method based on electrochemical oxidation technology |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| ASS | Succession or assignment of patent right |
Owner name: CHENGDU KAIMAI ENVIRONMENTAL PROTECTION TECHNOLOGY Free format text: FORMER OWNER: CHENGDU K + M METALS CO., LTD. Effective date: 20131121 |
|
| C41 | Transfer of patent application or patent right or utility model | ||
| COR | Change of bibliographic data |
Free format text: CORRECT: ADDRESS; FROM: 610500 CHENGDU, SICHUAN PROVINCE TO: 610041 CHENGDU, SICHUAN PROVINCE |
|
| TR01 | Transfer of patent right |
Effective date of registration: 20131121 Address after: Wuhou District Frasers road Chengdu city Sichuan province 610041 No. 511 1 4 storey building No. 34 Patentee after: Chengdu Kaimai Environmental Protection Technology Co., Ltd. Address before: 610500 New Industrial Road, Xindu Industrial District, Sichuan, Chengdu Patentee before: Chengdu K & M Metals Co., Ltd. |
|
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20111026 Termination date: 20180512 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |