CN207175697U - A kind of slaughterhouse wastewater treatment system of automatic pulp water separation - Google Patents
A kind of slaughterhouse wastewater treatment system of automatic pulp water separation Download PDFInfo
- Publication number
- CN207175697U CN207175697U CN201720748475.8U CN201720748475U CN207175697U CN 207175697 U CN207175697 U CN 207175697U CN 201720748475 U CN201720748475 U CN 201720748475U CN 207175697 U CN207175697 U CN 207175697U
- Authority
- CN
- China
- Prior art keywords
- water
- tank
- filtering ponds
- automatic pulp
- regulating reservoir
- 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
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims abstract description 50
- 238000000926 separation method Methods 0.000 title claims abstract description 9
- 238000004065 wastewater treatment Methods 0.000 title claims abstract description 9
- 238000001914 filtration Methods 0.000 claims abstract description 21
- 230000001105 regulatory Effects 0.000 claims abstract description 16
- 238000004659 sterilization and disinfection Methods 0.000 claims abstract description 12
- 238000004140 cleaning Methods 0.000 claims abstract description 10
- 239000003610 charcoal Substances 0.000 claims abstract description 9
- 230000001954 sterilising Effects 0.000 claims abstract description 9
- OKTJSMMVPCPJKN-UHFFFAOYSA-N carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 7
- 238000005276 aerator Methods 0.000 claims description 6
- 239000010865 sewage Substances 0.000 claims description 5
- 229910052799 carbon Inorganic materials 0.000 claims description 4
- 238000002156 mixing Methods 0.000 claims description 4
- 238000003756 stirring Methods 0.000 claims description 4
- 238000005660 chlorination reaction Methods 0.000 claims description 2
- 238000006385 ozonation reaction Methods 0.000 claims description 2
- 239000002351 wastewater Substances 0.000 abstract description 32
- 244000144972 livestock Species 0.000 abstract description 4
- 238000004064 recycling Methods 0.000 abstract description 4
- 238000010276 construction Methods 0.000 abstract description 2
- 239000002699 waste material Substances 0.000 abstract description 2
- 239000010802 sludge Substances 0.000 description 6
- 239000000725 suspension Substances 0.000 description 5
- 238000003307 slaughter Methods 0.000 description 4
- 230000000249 desinfective Effects 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- 239000005416 organic matter Substances 0.000 description 3
- 241000276438 Gadus morhua Species 0.000 description 2
- 244000052616 bacterial pathogens Species 0.000 description 2
- 230000033228 biological regulation Effects 0.000 description 2
- 235000019516 cod Nutrition 0.000 description 2
- 239000012535 impurity Substances 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 235000013372 meat Nutrition 0.000 description 2
- 229910052757 nitrogen Inorganic materials 0.000 description 2
- IJGRMHOSHXDMSA-UHFFFAOYSA-N nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 2
- 229910052760 oxygen Inorganic materials 0.000 description 2
- 239000001301 oxygen Substances 0.000 description 2
- MYMOFIZGZYHOMD-UHFFFAOYSA-N oxygen Chemical compound O=O MYMOFIZGZYHOMD-UHFFFAOYSA-N 0.000 description 2
- CBENFWSGALASAD-UHFFFAOYSA-N ozone Chemical compound [O-][O+]=O CBENFWSGALASAD-UHFFFAOYSA-N 0.000 description 2
- 239000002957 persistent organic pollutant Substances 0.000 description 2
- 229910052698 phosphorus Inorganic materials 0.000 description 2
- 241000251468 Actinopterygii Species 0.000 description 1
- 241000894006 Bacteria Species 0.000 description 1
- 210000004369 Blood Anatomy 0.000 description 1
- 208000010392 Bone Fractures Diseases 0.000 description 1
- 241000700605 Viruses Species 0.000 description 1
- 238000010521 absorption reaction Methods 0.000 description 1
- 238000005273 aeration Methods 0.000 description 1
- 238000006065 biodegradation reaction Methods 0.000 description 1
- 239000008280 blood Substances 0.000 description 1
- 230000001488 breeding Effects 0.000 description 1
- 235000012970 cakes Nutrition 0.000 description 1
- 230000015556 catabolic process Effects 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 230000000875 corresponding Effects 0.000 description 1
- 230000004059 degradation Effects 0.000 description 1
- 238000006731 degradation reaction Methods 0.000 description 1
- 230000000593 degrading Effects 0.000 description 1
- 230000029087 digestion Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 235000019688 fish Nutrition 0.000 description 1
- 239000003292 glue Substances 0.000 description 1
- 239000004519 grease Substances 0.000 description 1
- 238000000265 homogenisation Methods 0.000 description 1
- 238000006460 hydrolysis reaction Methods 0.000 description 1
- 230000003340 mental Effects 0.000 description 1
- 230000002906 microbiologic Effects 0.000 description 1
- 239000011368 organic material Substances 0.000 description 1
- 210000000056 organs Anatomy 0.000 description 1
- 230000020477 pH reduction Effects 0.000 description 1
- OAICVXFJPJFONN-UHFFFAOYSA-N phosphorus Chemical compound [P] OAICVXFJPJFONN-UHFFFAOYSA-N 0.000 description 1
- 239000011574 phosphorus Substances 0.000 description 1
- 244000144977 poultry Species 0.000 description 1
- 230000000717 retained Effects 0.000 description 1
- 238000004062 sedimentation Methods 0.000 description 1
- 150000003384 small molecules Chemical class 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 239000004071 soot Substances 0.000 description 1
Abstract
The utility model discloses a kind of slaughterhouse wastewater treatment system of automatic pulp water separation, including automatic pulp water separate tank, acidifying regulating reservoir, preaeration regulating reservoir, sbr reactor pond, cleaning filtering ponds, charcoal filtering ponds, accurate sterilization pool, reuse pool and sludge-tank.The utility model construction cost is low; it is compact-sized rationally, automaticity it is high, it is stable efficiently; it the processing such as can be efficiently separated, be filtered, being aoxidized, being decolourized, being sterilized to waste water; solves the situation that discharge of wastewater is difficult, discharge of wastewater is seriously polluted and not up to standard; waste water is turned waste into wealth simultaneously; waste water recyclable recycling, effectively save water resource, environmental protection and human and livestock health after row is handled.
Description
Technical field
Technical field of waste water processing is the utility model is related to, particularly a kind of slaughterhouse wastewater treatment system of automatic pulp water separation
System.
Background technology
During butchering with meat packing, to exclude containing blood stains, grease, hair, meat bits, livestock and poultry offal debris, not
The waste water of the polluters such as the foodstuff and excrement of digestion, such waste water have water is big, draining is uneven, concentration is high, impurity and
The features such as suspension is more, biodegradability is good, COD, BOD, N, P content are high, but also containing largely human health are harmful to micro-
Biology.Slaughtering wastewater such as directly discharges without processing, water environment can be caused seriously to pollute, human and livestock health damages.
Contained polluter belongs to the organic matter being readily biodegradable mostly in slaughtering wastewater, after they are discharged into water body,
The dissolved oxygen in water can be promptly consumed, causes fish and aquatile because of anoxic and dead;Because anoxic can also turn water body
It is changed into anaerobic state, can so makes water quality deterioration, produce stink, influence health.Meanwhile the pathogenic microorganisms in waste water can be a large amount of
Breeding, endangers people's health.Slaughtering wastewater is handled, removes its pollution, recycling to preserving the ecological environment and people
Class health is very necessary.
Utility model content
In order to overcome the disadvantages mentioned above of prior art, the purpose of this utility model is to provide a kind of rational in infrastructure, automation
Degree is high, stable efficient, effectively removes the slaughterhouse wastewater treatment of the automatic pulp water separation of contaminated wastewater and recycling
System.
Technical scheme is used by the utility model solves its technical problem：
A kind of slaughterhouse wastewater treatment system of automatic pulp water separation, wherein, including be sequentially connected by pipeline logical automatic
Pulp water separate tank, acidifying regulating reservoir, preaeration regulating reservoir, sbr reactor pond, cleaning filtering ponds, charcoal filtering ponds, accurate sterilization pool and
Reuse pool, in addition to sludge-tank, the sludge-tank are connected by pipeline with the automatic pulp water separate tank and sbr reactor pond；
The automatic pulp water separate tank bottom is provided with automatic slag-water separator, and mixing stirring device, institute are provided with the acidifying regulating reservoir
State preaeration regulating reservoir bottom and be provided with preaerator and sewage lifter, water decanter and bottom are provided with the sbr reactor pond
Portion is provided with aerator, and the cleaning filtering ponds include first filter chamber and secondary filter room, the filter chamber for the first time and secondary
Filter is respectively equipped with filter chamber, the charcoal filtering ponds are provided with carbon filter, ultraviolet is provided with the accurate sterilization pool
Chlorination equipment and ozonization plant, the reuse pool bottom are provided with recycle-water lifting device, and the sludge-tank is provided with press filtration
Machine.
As further improvement of the utility model：Sbr reactor pond side is provided with air blower, the air blower and institute
Preaerator is stated to connect with aerator.
Compared with prior art, the beneficial effects of the utility model are：
The utility model construction cost is low, it is rational in infrastructure, automaticity is high, it is stable efficiently, waste water can be entered
Row such as efficiently separates, filtered, aoxidizing, decolourizing, sterilize at the processing, and it is seriously polluted and not to solve discharge of wastewater hardly possible, discharge of wastewater
Situation up to standard, while waste water is turned waste into wealth, waste water recyclable recycling, effectively save water resource, protection after row is handled
Environment and human and livestock health.
Brief description of the drawings
Fig. 1 is structural representation of the present utility model.
Embodiment further illustrates in conjunction with brief description of the drawings with embodiment to the utility model：
As shown in Fig. 1, a kind of slaughterhouse wastewater treatment system of automatic pulp water separation, wherein, including by pipeline successively
The automatic pulp water separate tank 1 that is connected, acidifying regulating reservoir 2, preaeration regulating reservoir 3, sbr reactor pond 4, cleaning filtering ponds 5, charcoal mistake
Filter tank 6, accurate sterilization pool 7 and reuse pool 8, in addition to sludge-tank 9, the sludge-tank 9 pass through pipeline and the automatic pulp water
Separate tank 1 is connected with sbr reactor pond 4；The automatic bottom of pulp water separate tank 1 is provided with automatic slag-water separator 11, the acidifying
Mixing stirring device 21 is provided with regulating reservoir 2, the bottom of preaeration regulating reservoir 3 is provided with preaerator 31 and sewage lifting fills
32 are put, water decanter 41 is provided with the sbr reactor pond 4 and bottom is provided with aerator 42, the cleaning filtering ponds 5 include first
Filter chamber 51 and secondary filter room 52, it is described to be respectively equipped with the filter in filter chamber 51 and secondary filter room 52 for the first time
53, the charcoal filtering ponds 6 are provided with carbon filter 61, are provided with apparatus for ultraviolet disinfection 71 in the accurate sterilization pool 7 and ozone disappears
Malicious device 72, the bottom of reuse pool 8 are provided with recycle-water lifting device 81, and the sludge-tank 9 is provided with filter press 91.
The side of sbr reactor pond 4 is provided with air blower 43, and the air blower 43 fills with the preaerator 31 and aeration
Put 42 connections.
Operation principle of the present utility model：During operation, slaughtering wastewater sequentially enters automatic pulp water separate tank 1, acidifying regulation
Pond 2, preaeration regulating reservoir 3, sbr reactor pond 4, cleaning filtering ponds 5, charcoal filtering ponds 6, accurate sterilization pool 7 and reuse pool 8.
In automatic pulp water separate tank 1, the bulk debris automatic sedimentation such as internal organ, broken bone in waste water, automatic slag-water separator 11 removes useless
The fine suspensions such as hair, the dregs of fat in water, sediment drain into sludge-tank 9, reduce follow-up processing load, reduce operation processing
Cost；In regulating reservoir 2 is acidified, it is sufficiently stirred waste water and sludge by mixing stirring device 21, under the conditions of hydrolysis acidification,
Using facultative microbe, the larger molecular organics matter for being dissolved in water in waste water is resolved into small molecule organic material, by big portion
It is dissolved matter to divide insoluble organic matter degradation, improves the biodegradability of waste water, while reduce the sludge yield of system；Pre-
In aerating regulation pond 3, preaerator 31 makes waste water progress preaeration allow the raising of waste water dissolved oxygen and water quantity and quality to be equalized
Homogenization, some organic pollutants of degrading, to mitigate the processing load of follow-up aerobic section, is entered by sewage lifter 32
In sbr reactor pond 4；To in sbr reactor pond 4, by aerator 42, under aerobic condition, aerobic microbiological is utilized, activity is dirty
Mud method can remove the deliquescent and biochemical organic matter of colloidal state from sewage and can be by the suspension of activated sludge absorption
Solid and some other material, reduce COD, BOD value of waste water, while can also remove a part of phosphorus element and nitrogen, by processing
Waste water afterwards strains waste water under water condition and flows into cleaning filtering ponds 5, sludge is discharged into sludge-tank 9 through water decanter 41；In cleaning filtering ponds
In 5, waste water passes through first filter chamber 51 and secondary filter room 52 successively, by filter 53, suspension and glue in waste water
Body is retained in filter material surface and internal layer space, and filter water is discharged by outlet, and this method filter effect for repeating filtering is more
It is good, more impurity can be removed；In charcoal filtering ponds 6, by carbon filter 61, by the suction-operated of activated carbon, enter one
Step removes Organic Pollutants in Wastewater, suspension and colourity；In accurate sterilization pool 7, apparatus for ultraviolet disinfection 71 and ozone disappear
Malicious device 72 carries out disinfection to waste water, by the bacterium in water, virus removal；Discharge is passed through reuse pool 8 after standard water discharge, passes through
Recycle-water lifting device 81 connects each water place；Sludge-tank 9 passes through pipeline and automatic pulp water separate tank 1 and sbr reactor pond 4
Be connected, store sludge, by filter press 91 by sludge press filtration into mud cake deliver to soot landfill.
In summary, after one of ordinary skill in the art reads the utility model file, according to skill of the present utility model
Art scheme and technical concept make other various corresponding conversion schemes without creative mental labour, and it is new to belong to this practicality
The scope that type is protected.
Claims (2)
- A kind of 1. slaughterhouse wastewater treatment system of automatic pulp water separation, it is characterised in that：It is logical including being sequentially connected by pipeline Automatic pulp water separate tank, acidifying regulating reservoir, preaeration regulating reservoir, sbr reactor pond, cleaning filtering ponds, charcoal filtering ponds, accurate sterilization Pond and reuse pool, in addition to sludge-tank, the sludge-tank pass through pipeline and the automatic pulp water separate tank and sbr reactor pond phase Even；The automatic pulp water separate tank bottom is provided with automatic slag-water separator, and mixing stirring device is provided with the acidifying regulating reservoir, The preaeration regulating reservoir bottom is provided with preaerator and sewage lifter, be provided with the sbr reactor pond water decanter and Bottom is provided with aerator, and the cleaning filtering ponds include first filter chamber and secondary filter room, the first filter chamber and two Filter is respectively equipped with secondary filter chamber, the charcoal filtering ponds are provided with carbon filter, are provided with the accurate sterilization pool ultraviolet Line chlorination equipment and ozonization plant, the reuse pool bottom are provided with recycle-water lifting device, and the sludge-tank is provided with pressure Filter.
- A kind of 2. slaughterhouse wastewater treatment system of automatic pulp water separation according to claim 1, it is characterised in that：Institute State sbr reactor pond side and be provided with air blower, the air blower is connected with the preaerator and aerator.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720748475.8U CN207175697U (en) | 2017-06-26 | 2017-06-26 | A kind of slaughterhouse wastewater treatment system of automatic pulp water separation |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720748475.8U CN207175697U (en) | 2017-06-26 | 2017-06-26 | A kind of slaughterhouse wastewater treatment system of automatic pulp water separation |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN207175697U true CN207175697U (en) | 2018-04-03 |
Family
ID=61734230
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201720748475.8U Expired - Fee Related CN207175697U (en) | 2017-06-26 | 2017-06-26 | A kind of slaughterhouse wastewater treatment system of automatic pulp water separation |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN207175697U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108689550A (en) * | 2018-05-21 | 2018-10-23 | 李亮亮 | A kind of processing method of slaughterhouse sewage |
-
2017
- 2017-06-26 CN CN201720748475.8U patent/CN207175697U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108689550A (en) * | 2018-05-21 | 2018-10-23 | 李亮亮 | A kind of processing method of slaughterhouse sewage |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| 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: 20180403 Termination date: 20190626 |