CN205024039U - Effluent treatment plant slaughters - Google Patents
Effluent treatment plant slaughters Download PDFInfo
- Publication number
- CN205024039U CN205024039U CN201520624173.0U CN201520624173U CN205024039U CN 205024039 U CN205024039 U CN 205024039U CN 201520624173 U CN201520624173 U CN 201520624173U CN 205024039 U CN205024039 U CN 205024039U
- Authority
- CN
- China
- Prior art keywords
- basin
- connects
- catch
- equalizing tank
- catchments
- 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.)
- Expired - Fee Related
Links
Landscapes
- Water Treatment By Electricity Or Magnetism (AREA)
Abstract
The utility model relates to an environmental protection field especially relates to effluent treatment plant slaughters. Contain the catch -basin that catchments, the catch -basin that catchments contains butchers waste water and gets into the pipeline, contains the solid -liquid separation machine on the catch -basin that catchments, installs mixing pump on the catch -basin that catchments, and the catch -basin avris that catchments contains oil removal check slag bath, stretching out pipe connection equalizing basin and accident pond in the oil removal check slag bath respectively, installing the elevator pump on the accident pond, the elevator pump passes through the pipe connection rotary drum filter, and the rotary drum filter passes through pipe connection anaerobism device, and the equalizing basin is still connected to the rotary drum filter, and the equalizing basin is also connected to the anaerobism device, and the anaerobism device still passes through concentrated pond of pipe connection and desulfurizer, and marsh gas storage bag is still connected to the desulfurizer. Beneficial effect: simple structure, safe convenient, equipment drops into for a short time, and the denitrogenation effect is better.
Description
Technical field
The utility model relates to field of Environment Protection, particularly relates to slaughterhouse wastewater treatment device.
Background technology
Certain waste water can be produced, as the waste water such as flushing, ground flushing that disintegrate in slaughtering process.The materials such as the fat in these waste water, protein, without process, directly enter water body, will cause serious eutrophication to its surrounding water, the ability of committing suicide of havoc water body, cause water body to turn black and foul, affect environment and agricultural irrigation.
Utility model content
The object of utility model: in order to provide a kind of slaughterhouse wastewater treatment device of better effects if, specific purposes are shown in multiple substantial technological effects of concrete implementation section.
In order to reach as above object, the utility model takes following technical scheme:
Slaughterhouse wastewater treatment device, it is characterized in that, comprise the catch-basin that catchments, the catch-basin that catchments comprises slaughterhouse wastewater and enters pipeline, catchment on catch-basin and comprise solid-liquid separating machine, catchment on catch-basin and mixing pump is installed, the catch-basin avris that catchments comprises oil removal lattice slag bath, stretch out pipeline in described oil removal lattice slag bath respectively and connect equalizing tank and accident pool, accident pool is provided with lift pump, lift pump connects rotary drum filter by pipeline, rotary drum filter connects anaerobic device by pipeline, rotary drum filter also connects equalizing tank, anaerobic device also connects equalizing tank, anaerobic device also connects concentration basin and devulcanizer by pipeline, devulcanizer also connects biogas storage bag.
The further technical scheme of the utility model is, described anaerobic device is connected to deammonification tank, also comprise the Root's blower that can carry out air blast to deammonification tank, also comprise one-level light electrolysis biochemistry pool, one-level light electrolysis biochemistry pool connects equalizing tank and sludge thickener, one-level light electrolysis biochemistry pool is also connected to preliminary sedimentation tank, and preliminary sedimentation tank also connects equalizing tank and sludge settling; One-level light electrolysis biochemistry pool also connecting secondary light electrolysis biochemistry pool, secondary light electrolysis biochemistry pool connects equalizing tank and sludge settling, and equalizing tank is connected second pond with sludge settling, and second pond connects filtering basin.
The further technical scheme of the utility model is, described filtering basin connect equalizing tank and sludge thickener, and filtering basin also connect sterilization pool, and sterilization pool inside comprises chlorine dioxide generator, and sterilization pool connects discharge weir, and sterilization pool also connects equalizing tank and sludge thickener.
The further technical scheme of the utility model is, described sludge settling also comprises surge pump, and surge pump connects air compressor machine; Pressure filter is connected by pipeline below mud.
The further technical scheme of the utility model is, comprises agitator in described equalizing tank.
Adopt the utility model of as above technical scheme, have following beneficial effect relative to prior art: structure is simple, and safe ready, equipment investment is little, and denitrification effect is better.
Accompanying drawing explanation
In order to further illustrate the utility model, be described further below in conjunction with accompanying drawing:
Fig. 1 is structure iron first part;
Fig. 2 is structure iron second section;
Fig. 3 is structure iron Part III;
Fig. 4 is structure iron Part IV;
Fig. 5 is structure iron Part V;
Wherein: 1. catchment catch-basin; 2. solid-liquid separating machine; 3. oil removal lattice slag bath; 4. excavating pump; 5. accident pool; 6. lift pump; 7. rotary drum filter; 8. anaerobic device; 9. deammonification tank; 10. agitator; 11. equalizing tanks; 12. lift pumps; 13. sludge thickeners; 14. air compressor machines; 15. surge pumps; 16. pressure filter; 17. one-level light electrolysis biochemistry pools; 18. preliminary sedimentation tanks; 19. devulcanizers; 20. biogas storage bags; 21. pressure releasing devices; 22. secondary light electrolysis biochemistry pools; 23. second ponds; 24. filtering basin; 25. Root's blowers; 26. sterilization pools; 27. Chlorine Dioxide Oxidation devices; 28. discharge weirs.
Embodiment
Be described embodiment of the present utility model below in conjunction with accompanying drawing, embodiment does not form restriction of the present utility model:
Slaughterhouse wastewater treatment device, it is characterized in that, comprise the catch-basin 1 that catchments, the catch-basin 1 that catchments comprises slaughterhouse wastewater and enters pipeline, catchment on catch-basin 1 and comprise solid-liquid separating machine, catchment on catch-basin 1 and mixing pump is installed, catch-basin 1 avris that catchments comprises oil removal lattice slag bath 3, stretch out pipeline in described oil removal lattice slag bath 3 respectively and connect equalizing tank and accident pool, accident pool is provided with lift pump, lift pump connects rotary drum filter by pipeline, rotary drum filter connects anaerobic device by pipeline, rotary drum filter also connects equalizing tank, anaerobic device also connects equalizing tank, anaerobic device also connects concentration basin and devulcanizer by pipeline, devulcanizer also connects biogas storage bag.The technique effect of the essence that the technical scheme at this place plays and implementation procedure thereof are as follows: slaughterhouse wastewater enters the settling pit that catchments, stirred by mixing pump catchmenting in sedimentation basin, mixture after stirring enters solid-liquid separating machine, in solid-liquid separating machine, carry out solid be originally separated with liquid-based, entering oil removal lattice slag bath, in pond, be separated by proportion, then directly enter equalizing tank.Some enters accident pool, process further in accident pool, then lift pump is passed through, enter rotary drum filter (this filter can be separated the organism of more than 0.2mm), the organism separated enters UASB device (anaerobic device), and some directly enters equalizing tank from rotary drum filter, opens the valve of UASB device, water enters equalizing tank, and other mud enter concentration basin.From UASB device, isolated gas enters devulcanizer, carries out dosing desulfurization, enters biogas storage bag after desulfurization, biogas for subsequent use.
Described anaerobic device is connected to deammonification tank, also comprise the Root's blower that can carry out air blast to deammonification tank, also comprise one-level light electrolysis biochemistry pool, one-level light electrolysis biochemistry pool connects equalizing tank and sludge thickener, one-level light electrolysis biochemistry pool is also connected to preliminary sedimentation tank, and preliminary sedimentation tank also connects equalizing tank and sludge settling; One-level light electrolysis biochemistry pool also connecting secondary light electrolysis biochemistry pool, secondary light electrolysis biochemistry pool connects equalizing tank and sludge settling, and equalizing tank is connected second pond with sludge settling, and second pond connects filtering basin.The technique effect of the essence that the technical scheme at this place plays and implementation procedure thereof are as follows: do not obtain the part that processes from UASB device out, enter deammonification tank, deamination is carried out by air flowing, Root's blower works again in the process, the part of blowout ammonia enters equalizing tank and sludge sump, entering a light electrolysis biochemistry pool, carry out electrolysis, electrolysis rear portion enters equalizing tank and sludge thickener, the part of micro-electrolysis enters preliminary sedimentation tank, a part enters equalizing tank and sludge thickener thus, another part enters secondary light electrolysis biochemistry pool, carry out electrolysis again, a part enters equalizing tank and sludge thickener thus, another part enters second pond, again precipitate, again after precipitation, a second pond part is had to enter equalizing tank and sludge thickener, another part enters filtering basin, filter.
Described filtering basin connect equalizing tank and sludge thickener, and filtering basin also connect sterilization pool, and sterilization pool inside comprises chlorine dioxide generator, and sterilization pool connects discharge weir, and sterilization pool also connects equalizing tank and sludge thickener.The technique effect of the essence that the technical scheme at this place plays and implementation procedure thereof are as follows: the material after filtration, a part enters equalizing tank and mud settling pit, another part enters sterilization pool, is carried out disinfection by chlorine dioxide generator, and sterilization rear portion directly enters discharge weir.Another part enters equalizing tank and sludge thickener.UASB device is anaerobic device.
Described sludge settling also comprises surge pump, and surge pump connects air compressor machine; Pressure filter is connected by pipeline below mud.Agitator is comprised in described equalizing tank.The technique effect of the essence that the technical scheme at this place plays and implementation procedure thereof are as follows: the mud in sludge thickener, enter into air compressor machine by surge pump gas to process, mud enters pressure filter process, and water enters into equalizing tank, and the mud after process is waited for for subsequent use.Water in equalizing tank, is stirred by agitator, regulates in equalizing tank, waits for for subsequent use.
In a creative way, each effect above independently exists, and can also complete the combination of the above results with a nested structure.It is clear that the technique effect that above structure realizes realizes, if do not consider the technical scheme of adding, the utility model title can also be a kind of environmental protection structure.Not shown part details.
It should be noted that, multiple schemes that the utility model provides comprise general planning own, separate, mutually do not restrict, but it also can combine when not conflicting mutually, reaching multiple effect and jointly realizing.
Light electrolysis mechanism:
Based on holey polymer carrier as microbe carrier, ferrous as flocculation agent based on employing again, iron is active metal, the physics in redox processes and easily caused by generation metallic corrosion electrochemistry, chemistry, electrochemistry comprehensive action, thus forms light electrolysis.In recent years, adopt the research report of micro-electrolysis treatment RE waste water, Metallurgical Waste Water, coke-oven waste water, pharmacy waste water, electroplating wastewater, oil, wastewater from chemical industry, gas washing wastewater, dyeing waste water, agricultural chemicals waste water etc. more and more.The feature of various organic industrial sewage is that pollutant kind is many above, and toxicity is large, and COD value is high, and acid-basicity change is strong, and major part is all the pollution substance of bio-refractory, has very large harm to ecotope and HUMAN HEALTH.If adopt biochemical method or other this type of waste water of single-item handling technical finesse, not only uneconomical economically, be also difficult to reach good treatment effect simultaneously.The weak electrolysis mechanism that micro-electrolysis stuffing is formed combines with biochemical processing process then improving wastewater biodegradability, improves waste water quality, alleviates subsequent disposal load and improve treatment effect aspect to have obvious advantage.Micro-electrolysis treatment trade effluent is utilized to have the advantages such as the treatment of wastes with processes of wastes against one another, effective, reduced investment, widely applicable and running cost is low because of it and extensively come into one's own.Its light electrolysis mechanism is as follows: the ultimate principle of Fe-C micro electrolysis reaction is that iron and charcoal form galvanic cell in electrolyte solution, iron is anode, charcoal is negative electrode, anode shows as in cell reaction that to lose electronics oxidized, and negative electrode obtains electronics is reduced, Fe-C micro electrolysis contacts based on the battery in electrochemistry and cathode material, is immersed in electric cell reaction and becomes corrosion cell, and metal anode electrode reaction is as follows: anode (Fe): Fe+2e → Fe
2+e
0(Fe
2+/ Fe)=-0.44V negative electrode (C): under acidic conditions, 2H++2e → 2 [H] →+H
2e
0(H
+/ H
2)=0.00V is when there being dissolved oxygen to exist, and under acidic conditions, reaction shows as: O
2+ 4H++4e → 2H
2oE
0(O
2)=1.23V is when having dissolved oxygen to exist, under alkaline condition: O
2+ 2H
2o+4e → 4OH
-e
0(O
2/ OH
-)=0.40V is from cathodic reaction, under acid aerobic condition, both potential differences are larger, corrosion reaction is carried out the fastest, this effect illustrating that iron processes industrial organic waste water under reduction aeration condition should be better than the treatment effect under not aeration condition, in addition, cathodic reaction consumes a large amount of H, can improve the pH value of solution.1. the nascent state ［ H ］ obtained in the redoxomorphism electrode reaction of hydrogen has very strong activity, can with NO in waste water
2 --N, NO
3 -there is reductive action in-N.The hydrogen in statu nascendi produced in electrochemical reaction has larger activity, the chromonic structures of chromonic material can be destroyed, some organic chromophoric group and auxochrome group in waste water are broken, macromole is decomposed into small molecules, reaching the object of decolouring, making the composition of waste water change to being easy to biochemical direction simultaneously.2. the reductive action iron of iron is active metal, in the waste water under acidity or slant acidity condition, occurs to react as follows: Fe+2H
+→ Fe
2++ H
2when there being oxygenant in water, Fe
2+fe can be oxidized to further
3+, its reaction formula is: Fe
2+-e → Fe
3+from above formula, some macromole color development organic matter degradations can be made under acidic conditions to be lower-molecular substance that is colourless or light color, to there is decolorization, also improve the biodegradability of waste water simultaneously, for subsequent biochemical process creates condition.3. the Fe that obtains from anode of the coagulation of iron ion
2+under aerobic and alkaline condition, Fe (OH) can be generated
2with Fe (OH)
3, its reaction occurred is: Fe
2++ 2OH → Fe (OH)
24Fe
2++ 8OH+O
2+ 2H
2o → 4Fe (OH)
3the Fe (OH) generated
2be a kind of flocculation agent efficiently, there is good decolouring and adsorption.And the Fe (OH) generated
3also be a kind of efficient colloid flocculation agent, than the Fe (OH) that general medicament hydrolysis method obtains
3high adsorption capacity, can the insolubles that produces of suspended substance, part coloring matter and light electrolysis in strong adsorption waste water.Through the comprehensive action of above each reaction, finally realize following effect.(1) at pH, Fe/C(mass ratio) and the reaction times control suitable time, following reaction can be realized: NO
2 -+ 4H
++ 3e → 1/2N
2+ 2H
2oNO
3 -+ 6H
++ 5e → 1/2N
2+ 3H
2o(2) controlled not at that time at pH, Fe/C and reaction times, will react as follows: NO
2 -+ 8H
++ 6e → NH
4 ++ 2H
2oNO
3 -+ 10H
++ 8e → NH
4 ++ 3H
2o is from above formula, and light electrolysis has very excellent effect for slaughterhouse wastewater treatment.
more than show and describe ultimate principle of the present utility model, principal character and advantage of the present utility model.Those skilled in the art should understand the utility model and not be restricted to the described embodiments; what describe in above-described embodiment and specification sheets just illustrates principle of the present utility model; under the prerequisite not departing from the utility model spirit and scope; the utility model also has various changes and modifications, and these changes and improvements all fall in claimed scope.
Claims (5)
1. slaughterhouse wastewater treatment device, it is characterized in that, comprise the catch-basin that catchments (1), the catch-basin (1) that catchments comprises slaughterhouse wastewater and enters pipeline, catchment on catch-basin (1) and comprise solid-liquid separating machine, catchment on catch-basin (1) and mixing pump is installed, catch-basin (1) avris that catchments comprises oil removal lattice slag bath (3), stretch out pipeline in described oil removal lattice slag bath (3) respectively and connect equalizing tank and accident pool, accident pool is provided with lift pump, lift pump connects rotary drum filter by pipeline, rotary drum filter connects anaerobic device by pipeline, rotary drum filter also connects equalizing tank, anaerobic device also connects equalizing tank, anaerobic device also connects concentration basin and devulcanizer by pipeline, devulcanizer also connects biogas storage bag.
2. slaughterhouse wastewater treatment device as claimed in claim 1, it is characterized in that, described anaerobic device is connected to deammonification tank, also comprise the Root's blower that can carry out air blast to deammonification tank, also comprise one-level light electrolysis biochemistry pool, one-level light electrolysis biochemistry pool connects equalizing tank and sludge thickener, and one-level light electrolysis biochemistry pool is also connected to preliminary sedimentation tank, and preliminary sedimentation tank also connects equalizing tank and sludge settling; One-level light electrolysis biochemistry pool also connecting secondary light electrolysis biochemistry pool, secondary light electrolysis biochemistry pool connects equalizing tank and sludge settling, and equalizing tank is connected second pond with sludge settling, and second pond connects filtering basin.
3. slaughterhouse wastewater treatment device as claimed in claim 2, is characterized in that, described filtering basin connect equalizing tank and sludge thickener, filtering basin also connect sterilization pool, sterilization pool inside comprises chlorine dioxide generator, and sterilization pool connects discharge weir, and sterilization pool also connects equalizing tank and sludge thickener.
4. slaughterhouse wastewater treatment device as claimed in claim 2, it is characterized in that, described sludge settling also comprises surge pump, and surge pump connects air compressor machine; Pressure filter is connected by pipeline below mud.
5. slaughterhouse wastewater treatment device as claimed in claim 2, is characterized in that, comprise agitator in described equalizing tank.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520624173.0U CN205024039U (en) | 2015-08-19 | 2015-08-19 | Effluent treatment plant slaughters |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520624173.0U CN205024039U (en) | 2015-08-19 | 2015-08-19 | Effluent treatment plant slaughters |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205024039U true CN205024039U (en) | 2016-02-10 |
Family
ID=55256589
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201520624173.0U Expired - Fee Related CN205024039U (en) | 2015-08-19 | 2015-08-19 | Effluent treatment plant slaughters |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN205024039U (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106746148A (en) * | 2017-03-17 | 2017-05-31 | 成都源蓉科技有限公司 | A kind of magnetic loading precipitation filtration, purification system |
| CN110143723A (en) * | 2019-05-25 | 2019-08-20 | 宁波翼宇汽车零部件有限公司 | A kind of sewage water treatment method |
| CN111285550A (en) * | 2020-03-11 | 2020-06-16 | 东莞市粤绿环保有限公司 | Garbage leachate micro-electrolysis membrane method integrated treatment equipment for garbage transfer station |
| CN118307137A (en) * | 2024-03-22 | 2024-07-09 | 西南大学 | Microbial fuel cell coupling constructed wetland device and operation method |
-
2015
- 2015-08-19 CN CN201520624173.0U patent/CN205024039U/en not_active Expired - Fee Related
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106746148A (en) * | 2017-03-17 | 2017-05-31 | 成都源蓉科技有限公司 | A kind of magnetic loading precipitation filtration, purification system |
| CN110143723A (en) * | 2019-05-25 | 2019-08-20 | 宁波翼宇汽车零部件有限公司 | A kind of sewage water treatment method |
| CN111285550A (en) * | 2020-03-11 | 2020-06-16 | 东莞市粤绿环保有限公司 | Garbage leachate micro-electrolysis membrane method integrated treatment equipment for garbage transfer station |
| CN118307137A (en) * | 2024-03-22 | 2024-07-09 | 西南大学 | Microbial fuel cell coupling constructed wetland device and operation method |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN102010107B (en) | Treatment and cyclic utilization device and method of tannery wastewater | |
| CN101734817B (en) | Method for treating organic chemical waste water | |
| CN205933558U (en) | Processing apparatus of waste water | |
| CN101088938B (en) | Process of treating heavy metal containing sewage | |
| Cho et al. | Effects of electric voltage and sodium chloride level on electrolysis of swine wastewater | |
| CN206142964U (en) | Integration high concentration sewage advanced oxidation treatment equipment | |
| CN102701496A (en) | Method and process for treating high-concentration organic wastewater difficult to degrade | |
| CN205024039U (en) | Effluent treatment plant slaughters | |
| CN107176760A (en) | A kind of high salt advance for the treatment of process of cyanide-bearing effluent and processing system | |
| CN207375910U (en) | A kind of processing system of landfill leachate | |
| CN106800356A (en) | A kind of advanced treatment of wastewater regeneration device based on biochemical and electrolysis tech | |
| CN209957618U (en) | Medicine comprehensive wastewater treatment system | |
| CN109264834A (en) | A kind of processing method and reactor of the nitrogenous organic wastewater with difficult degradation thereby containing chlorine | |
| CN102249501B (en) | Device and method for treating wastewater produced by hair-product manufacturing | |
| CN107777830A (en) | A kind of high-concentration hardly-degradable pharmacy wastewater treatment method and system | |
| CN208071546U (en) | A kind of chemical wastewater treatment standard emission system | |
| CN105084666A (en) | Chemical industry wastewater comprehensive treatment method | |
| CN103936208A (en) | Efficient micro-electrolysis multiphase flow air flotation reactor | |
| CN108358394A (en) | A kind of Novel dephosphorization sewage treatment process | |
| CN113860645A (en) | Method for treating high-concentration degradation-resistant organic wastewater | |
| CN109502911A (en) | A kind of sewage water treatment method | |
| KR19990026365A (en) | Wastewater Treatment Method and Apparatus by Fenton Oxidation and Electric Electrolysis | |
| CN1328181C (en) | Treater of sewage by electrochemistr catalyzing oxidizing | |
| CN106467349B (en) | High-concentration acidic organic wastewater treatment system and method | |
| CN105060656B (en) | Biochemical system auxiliary device and application thereof |
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: 20160210 Termination date: 20160819 |