CN204981521U - Processing system of pickles waste water - Google Patents
Processing system of pickles waste water Download PDFInfo
- Publication number
- CN204981521U CN204981521U CN201520757912.3U CN201520757912U CN204981521U CN 204981521 U CN204981521 U CN 204981521U CN 201520757912 U CN201520757912 U CN 201520757912U CN 204981521 U CN204981521 U CN 204981521U
- Authority
- CN
- China
- Prior art keywords
- pond
- fluid inlet
- heavy
- liquid outlet
- communicated
- 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.)
- Active
Links
Landscapes
- Purification Treatments By Anaerobic Or Anaerobic And Aerobic Bacteria Or Animals (AREA)
Abstract
The utility model discloses a processing system of pickles waste water, including thin grid pond, rotary drum grid machine, oil interceptor, equalizing basin, ABR anaerobism pond, detest the biochemical pond in heavy pond, AO sink in, pond, reaction tank, three sink pond, sludge tihckener and pressure filters. The utility model discloses stable and the easy operation of operation, the management is convenient, and the treatment effect is good, when removing organic matter removal, has higher slagging -off, oil removal, denitrogenation, dephosphorization function, goes out hydroenergy and enough reaches GB8979 -1996 one -level emission standard.
Description
Technical field
The utility model belongs to technical field of sewage, is specifically related to a kind of pickle wastewater treatment system.
Background technology
Pickles enterprise factory effluent mainly comprises the salt marsh waste water of salinity >5% and the daily production comprehensive wastewater of less salt, has the feature of high suspended matter, high oil, high salt, high ammonia nitrogen, high phosphorus, high density.
In prior art, the treatment system of pickle wastewater considers imperfection, pretreatment stage generally arranges grating tank, solid suspension larger in waste water is removed in interception, mostly do not consider to arrange the facility removing dish slice, chilli seed particle and oil removing, cause the normal operation having a strong impact on subsequent disposal facility, affect treatment effect; In addition, pickle wastewater belongs to high ammonia nitrogen, high phosphorus waste water, and the biochemical process of great majority employing at present, is difficult to make water outlet completely up to standard.
Utility model content
The purpose of this utility model is just to provide a kind of pickle wastewater treatment system to solve the problem.
The utility model is achieved through the following technical solutions above-mentioned purpose:
A kind for the treatment of system of pickle wastewater, comprise fine fack pond, Barrate type grilling machine, oil trap, equalizing tank, ABR anaerobic pond, detest heavy pond, A/O biochemistry pool, medium sediment pool, reaction tank, three heavy ponds, sludge thickener and pressure filter, the fluid inlet in described fine fack pond simultaneously with salt marsh pond and comprehensive wastewater pipeline communication, the liquid outlet in described fine fack pond is communicated with the fluid inlet of described Barrate type grilling machine, the liquid outlet of described Barrate type grilling machine is communicated with the fluid inlet of described oil trap, the liquid outlet of described oil trap is communicated with the fluid inlet of described equalizing tank, the liquid outlet of described equalizing tank is communicated with the fluid inlet of described ABR anaerobic pond, the liquid outlet of described ABR anaerobic pond is communicated with the described fluid inlet detesting heavy pond, the described liquid outlet detesting heavy pond is communicated with the fluid inlet of described A/O biochemistry pool, the liquid outlet of described A/O biochemistry pool is communicated with the fluid inlet of described medium sediment pool, the liquid outlet of described medium sediment pool is communicated with the fluid inlet of described reaction tank, the liquid outlet of described reaction tank is communicated with the fluid inlet in described three heavy ponds, the liquid outlet in described three heavy ponds is qualified discharge mouth, describedly detest between heavy pond and described ABR anaerobic pond, return flow line is provided with between described medium sediment pool and described A/O biochemistry pool, described three heavy ponds, described medium sediment pool and the described mud discharging mouth detesting heavy pond all lead to described sludge thickener, the discharge port of described sludge thickener leads to described pressure filter, the supernatant liquor relief outlet of described sludge thickener and the filtrate relief outlet of described pressure filter all lead to described equalizing tank.
Further, described fine fack pond adopts mechanical fine fack structure, and grizzly bar distance is 5 ~ 10mm, and the pitch of described Barrate type grilling machine is 0.5mm.
Further, reactor in described ABR anaerobic pond adopts the anaerobic baffled reactor of built-in two meters of elastic fillers, described detest in heavy pond and described medium sediment pool be provided with sludge reflux pump, the described sludge reflux pump outlet detesting heavy pond leads to described ABR anaerobic pond by return flow line, and the sludge reflux pump outlet of described medium sediment pool leads to described A/O biochemistry pool by return flow line.
Further, described A/O biochemistry pool adopts the structure of three sections of anoxics and aerobic treatment, arranges stirring mechanism in the oxygen-starved area of described A/O biochemistry pool.
Further, be provided with stirring mechanism in described reaction tank and add and have bodied ferric sulfate to carry out chemical dephosphorization as dephosphorization agent.
The beneficial effects of the utility model are:
The utility model is stable and simple to operate, convenient management, and treatment effect is good, and while organics removal, have higher slagging-off, oil removal, denitrogenation, phosphorus removal functional, water outlet can reach GB8979-1996 first discharge standard.
Accompanying drawing explanation
Fig. 1 is the structured flowchart of pickle wastewater treatment system described in the utility model.
Embodiment
Below in conjunction with accompanying drawing, the utility model is described in further detail:
As shown in Figure 1, the utility model comprises fine fack pond, Barrate type grilling machine, oil trap, equalizing tank, ABR anaerobic pond, detest heavy pond, A/O biochemistry pool, medium sediment pool, reaction tank, three heavy ponds, sludge thickener and pressure filter, the fluid inlet in fine fack pond simultaneously with salt marsh pond and comprehensive wastewater pipeline communication, the liquid outlet in fine fack pond is communicated with the fluid inlet of Barrate type grilling machine, the liquid outlet of Barrate type grilling machine is communicated with the fluid inlet of oil trap, the liquid outlet of oil trap is communicated with the fluid inlet of equalizing tank, the liquid outlet of equalizing tank is communicated with the fluid inlet of ABR anaerobic pond, the liquid outlet of ABR anaerobic pond is communicated with the fluid inlet detesting heavy pond, the liquid outlet detesting heavy pond is communicated with the fluid inlet of A/O biochemistry pool, the liquid outlet of A/O biochemistry pool is communicated with the fluid inlet of medium sediment pool, the liquid outlet of medium sediment pool is communicated with the fluid inlet of reaction tank, the liquid outlet of reaction tank is communicated with the fluid inlet in three heavy ponds, the liquid outlet in three heavy ponds is qualified discharge mouth, detest between heavy pond and ABR anaerobic pond, return flow line is provided with between medium sediment pool and A/O biochemistry pool, three heavy ponds, medium sediment pool all leads to sludge thickener with the mud discharging mouth detesting heavy pond, the discharge port of sludge thickener leads to pressure filter, the supernatant liquor relief outlet of sludge thickener and the filtrate relief outlet of pressure filter all lead to equalizing tank.
Pickle wastewater treatment system described in the utility model, fine fack pond adopts mechanical fine fack structure, and grizzly bar distance is 5 ~ 10mm, and the pitch of Barrate type grilling machine is 0.5mm.Reactor in ABR anaerobic pond adopts the anaerobic baffled reactor of built-in two meters of elastic fillers, detest in heavy pond and medium sediment pool and be provided with sludge reflux pump, the sludge reflux pump outlet detesting heavy pond leads to ABR anaerobic pond by return flow line, and the sludge reflux pump outlet of medium sediment pool leads to A/O biochemistry pool by return flow line.A/O biochemistry pool adopts the structure of three sections of anoxics and aerobic treatment, arranges stirring mechanism in the oxygen-starved area of A/O biochemistry pool.Being provided with stirring mechanism in reaction tank and adding has bodied ferric sulfate to carry out chemical dephosphorization as dephosphorization agent.
Working process of the present utility model is as follows:
The dense water of salinity >5% in salt marsh pond will be stored in, quantitatively fine fack pond is entered together with daily production comprehensive wastewater with pump daily means, waste water after mechanical fine fack removing macrobead suspended substance removes a large amount of pickles silk and chilli seed particle from flowing into Barrate type grilling machine, then water outlet passes through oil trap successively, equalizing tank, reach oil removal and regulating water quality respectively, the effect of the water yield, after homogeneous waste water by pump delivery to ABR anaerobic pond, anerobe is utilized to carry out anaerobic treatment, the water outlet of ABR anaerobic pond detests heavy pond mud-water separation from flowing into, detest sinking pool effluent and flow into A/O biochemistry pool, adopt three sections of anoxics, aerobic treatment, anoxic pond arranges stirring, Aerobic Pond adopts biological contact oxidation process, carry out biological carbon and phosphorous removal and organics removal process, water outlet is from flowing into medium sediment pool mud-water separation, medium sediment pool water outlet enters reaction tank and adds dephosphorization agent and PAM carries out chemical dephosphorization, flow into three heavy ponds after flocculation reaction and carry out solid-liquid separation, supernatant liquor qualified discharge.
The mud of the excess sludge and three heavy ponds generations of detesting heavy pond and medium sediment pool generation enters sludge thickener and concentrates, and supernatant liquor is back to equalizing tank, and the mud after concentrated transports outward disposal after carrying out processed, and pressing filtering liquid is back to equalizing tank.
Embodiment:
Water-quality guideline: pH value 5.5 ~ 7.5, CODCr2000 ~ 3000mg/L, ammonia nitrogen 30 ~ 60mg/L, total phosphorus 6 ~ 10mg/L, vegetable and animals oils 50 ~ 100mg/L, suspended substance 300 ~ 500mg/L, salinity 5000 ~ 8000mg/L.
The dense water of salinity >5% in salt marsh pond will be stored in, quantitatively fine fack pond is entered together with daily production comprehensive wastewater with pump daily means, machinery fine fack interval of grid strip adopts 5mm, waste water after grid removing macrobead suspended substance removes a large amount of pickles silk and chilli seed particle from flowing into Barrate type grilling machine, Barrate type grilling machine pitch adopts 0.5mm, then water outlet flows into oil trap, equalizing tank is flowed into after stopping 0.5h, residence time 12h, regulating water quality, after the water yield waste water by pump delivery to ABR anaerobic pond, anerobe is utilized to carry out anaerobic treatment, after stopping 24h, water outlet detests heavy pond mud-water separation from flowing into, precipitation 1.8h, water outlet flows into A/O biochemistry pool, after 36h, water outlet is from flowing into medium sediment pool mud-water separation, precipitation 1.8h, water outlet enters reaction tank and adds bodied ferric sulfate and PAM carries out, three heavy ponds are flowed into after coagulating 0.5h, water outlet after solid-liquid separation 1.5h, effluent quality after process: pH value 6 ~ 9, CODCr30 ~ 60mg/L, ammonia nitrogen 0.5 ~ 8mg/L, total phosphorus 0.1 ~ 0.5mg/L, vegetable and animals oils 1 ~ 3mg/L, all meets emission standard.
The mud of the excess sludge and three heavy ponds generations of detesting heavy pond and medium sediment pool generation enters sludge thickener and concentrates, and supernatant liquor is back to equalizing tank, and the mud after concentrated transports outward disposal after carrying out processed, and pressing filtering liquid is back to equalizing tank.
These are only preferred embodiment of the present utility model, not in order to limit the utility model, all do within spirit of the present utility model and principle any amendment, equivalent to replace and improvement etc., all should be included in protection domain of the present utility model.
Claims (5)
1. the treatment system of a pickle wastewater, it is characterized in that: comprise fine fack pond, Barrate type grilling machine, oil trap, equalizing tank, ABR anaerobic pond, detest heavy pond, A/O biochemistry pool, medium sediment pool, reaction tank, three heavy ponds, sludge thickener and pressure filter, the fluid inlet in described fine fack pond simultaneously with salt marsh pond and comprehensive wastewater pipeline communication, the liquid outlet in described fine fack pond is communicated with the fluid inlet of described Barrate type grilling machine, the liquid outlet of described Barrate type grilling machine is communicated with the fluid inlet of described oil trap, the liquid outlet of described oil trap is communicated with the fluid inlet of described equalizing tank, the liquid outlet of described equalizing tank is communicated with the fluid inlet of described ABR anaerobic pond, the liquid outlet of described ABR anaerobic pond is communicated with the described fluid inlet detesting heavy pond, the described liquid outlet detesting heavy pond is communicated with the fluid inlet of described A/O biochemistry pool, the liquid outlet of described A/O biochemistry pool is communicated with the fluid inlet of described medium sediment pool, the liquid outlet of described medium sediment pool is communicated with the fluid inlet of described reaction tank, the liquid outlet of described reaction tank is communicated with the fluid inlet in described three heavy ponds, the liquid outlet in described three heavy ponds is qualified discharge mouth, describedly detest between heavy pond and described ABR anaerobic pond, return flow line is provided with between described medium sediment pool and described A/O biochemistry pool, described three heavy ponds, described medium sediment pool and the described mud discharging mouth detesting heavy pond all lead to described sludge thickener, the discharge port of described sludge thickener leads to described pressure filter, the supernatant liquor relief outlet of described sludge thickener and the filtrate relief outlet of described pressure filter all lead to described equalizing tank.
2. the treatment system of pickle wastewater according to claim 1, is characterized in that: described fine fack pond adopts mechanical fine fack structure, and grizzly bar distance is 5 ~ 10mm, and the pitch of described Barrate type grilling machine is 0.5mm.
3. the treatment system of pickle wastewater according to claim 1, it is characterized in that: the reactor in described ABR anaerobic pond adopts the anaerobic baffled reactor of built-in two meters of elastic fillers, described detest in heavy pond and described medium sediment pool be provided with sludge reflux pump, the described sludge reflux pump outlet detesting heavy pond leads to described ABR anaerobic pond by return flow line, and the sludge reflux pump outlet of described medium sediment pool leads to described A/O biochemistry pool by return flow line.
4. the treatment system of pickle wastewater according to claim 1, is characterized in that: described A/O biochemistry pool adopts the structure of three sections of anoxics and aerobic treatment, arranges stirring mechanism in the oxygen-starved area of described A/O biochemistry pool.
5. the treatment system of pickle wastewater according to claim 1, is characterized in that: being provided with stirring mechanism in described reaction tank and adding has bodied ferric sulfate to carry out chemical dephosphorization as dephosphorization agent.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520757912.3U CN204981521U (en) | 2015-09-28 | 2015-09-28 | Processing system of pickles waste water |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520757912.3U CN204981521U (en) | 2015-09-28 | 2015-09-28 | Processing system of pickles waste water |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN204981521U true CN204981521U (en) | 2016-01-20 |
Family
ID=55115908
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201520757912.3U Active CN204981521U (en) | 2015-09-28 | 2015-09-28 | Processing system of pickles waste water |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN204981521U (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107162649A (en) * | 2017-05-27 | 2017-09-15 | 遵义盛林农业发展有限公司 | A kind of blueberry plantation irrigation water and its compound method |
| CN107892440A (en) * | 2017-12-04 | 2018-04-10 | 青岛市黎明水处理设备有限公司 | A kind of pickles, the full reuse treatment process of salted vegetables high-salinity wastewater zero-emission |
| CN109734252A (en) * | 2019-03-07 | 2019-05-10 | 四川舜瑞环境科技有限公司 | A kind of system and method handling pickle wastewater |
-
2015
- 2015-09-28 CN CN201520757912.3U patent/CN204981521U/en active Active
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107162649A (en) * | 2017-05-27 | 2017-09-15 | 遵义盛林农业发展有限公司 | A kind of blueberry plantation irrigation water and its compound method |
| CN107892440A (en) * | 2017-12-04 | 2018-04-10 | 青岛市黎明水处理设备有限公司 | A kind of pickles, the full reuse treatment process of salted vegetables high-salinity wastewater zero-emission |
| CN109734252A (en) * | 2019-03-07 | 2019-05-10 | 四川舜瑞环境科技有限公司 | A kind of system and method handling pickle wastewater |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN101264946B (en) | Iron-carbon pipe component capable of purifying waste water, integrated magnetoelectric oxidation biological filter chamber and application system | |
| CN204151203U (en) | A kind of dangerous waste disposal center Waste Water Treatment | |
| CN203392984U (en) | Bio-contact oxidation integrated sewage treatment system | |
| CN206767868U (en) | A kind of garbage percolation liquid treating system | |
| CN103508637B (en) | Traditional Chinese medicine wastewater treatment system and method for treating traditional Chinese medicine wastewater | |
| CN205133286U (en) | Full automatic processing equipment of nickeliferous waste water of high concentration | |
| CN104445837A (en) | Industrial combined wastewater bio-augmentation treatment system and method | |
| CN204981521U (en) | Processing system of pickles waste water | |
| CN109133524A (en) | The processing system and processing method of high COD medicine intermediate wastewater from chemical industry with high salt | |
| CN102180568B (en) | Integrated combined-type rural domestic sewage treatment device | |
| CN105565590A (en) | Advanced treatment system of high-concentration methanol wastewater by DAT-IAT (demand aeration tank-intermittent aeration tank) technique | |
| CN205347102U (en) | Degree of depth processing system of direct liquefaction of coal sewage | |
| CN211712893U (en) | Difficult degradation industrial waste water treatment system | |
| CN103435158A (en) | Method for reinforcing phosphorus removal and membrane pollution delaying of MBR | |
| CN202099169U (en) | Device for advanced treatment of secondary effluent in municipal sewage plant | |
| CN112960861A (en) | Biological denitrification treatment process for stainless steel pickling wastewater | |
| CN105174567B (en) | A kind of heavy metal containing wastewater treatment and recovery system and method | |
| CN202297284U (en) | Automatic control device for clean water treatment | |
| CN201990563U (en) | Integrated equipment used for advanced treatment of coking wastewater | |
| CN204752494U (en) | Sewage treatment system of hospital | |
| CN203440210U (en) | Wastewater treatment system for pharmaceutical factory | |
| CN102417278B (en) | Ecological wetland treatment system for treating industrial tail water | |
| CN205258241U (en) | Printing and dyeing wastewater treatment system | |
| CN205011582U (en) | Offal drainage | |
| CN203754501U (en) | Built-in anoxic aerated filter |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CB03 | Change of inventor or designer information |
Inventor after: Deng Jiaqing Inventor after: Hu Wenjun Inventor after: Hu Xiaohua Inventor before: Deng Jiaqing Inventor before: Hu Wenhua Inventor before: Hu Xiaohua |
|
| COR | Change of bibliographic data |