CN205974187U - Waste water integrated treating equipment raises pigs - Google Patents
Waste water integrated treating equipment raises pigs Download PDFInfo
- Publication number
- CN205974187U CN205974187U CN201620932930.5U CN201620932930U CN205974187U CN 205974187 U CN205974187 U CN 205974187U CN 201620932930 U CN201620932930 U CN 201620932930U CN 205974187 U CN205974187 U CN 205974187U
- Authority
- CN
- China
- Prior art keywords
- water
- sludge
- pipeline
- intaking valve
- aeration tube
- 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
- 239000002351 wastewater Substances 0.000 title claims abstract description 45
- 241000282887 Suidae Species 0.000 title abstract description 5
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 83
- 238000005273 aeration Methods 0.000 claims abstract description 52
- 239000007788 liquid Substances 0.000 claims abstract description 30
- 239000010802 sludge Substances 0.000 claims abstract description 28
- 230000007062 hydrolysis Effects 0.000 claims abstract description 27
- 238000006460 hydrolysis reaction Methods 0.000 claims abstract description 27
- 238000004065 wastewater treatment Methods 0.000 claims abstract description 27
- 238000004659 sterilization and disinfection Methods 0.000 claims abstract description 21
- JEGUKCSWCFPDGT-UHFFFAOYSA-N h2o hydrate Chemical compound O.O JEGUKCSWCFPDGT-UHFFFAOYSA-N 0.000 claims abstract description 20
- 238000006243 chemical reaction Methods 0.000 claims abstract description 15
- 239000007787 solid Substances 0.000 claims abstract description 12
- 239000003814 drug Substances 0.000 claims abstract description 7
- 206010021143 Hypoxia Diseases 0.000 claims abstract description 3
- 230000020477 pH reduction Effects 0.000 claims description 27
- 230000001954 sterilising effect Effects 0.000 claims description 20
- 230000001105 regulatory effect Effects 0.000 claims description 16
- 238000005276 aerator Methods 0.000 claims description 14
- 239000000047 product Substances 0.000 claims description 14
- 239000000945 filler Substances 0.000 claims description 11
- 239000012528 membrane Substances 0.000 claims description 11
- 238000000034 method Methods 0.000 claims description 10
- 238000004140 cleaning Methods 0.000 claims description 9
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 4
- 206010002660 Anoxia Diseases 0.000 claims description 2
- 241000976983 Anoxia Species 0.000 claims description 2
- 230000007953 anoxia Effects 0.000 claims description 2
- 239000007795 chemical reaction product Substances 0.000 claims 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 abstract description 3
- 239000001301 oxygen Substances 0.000 abstract description 3
- 229910052760 oxygen Inorganic materials 0.000 abstract description 3
- 238000000926 separation method Methods 0.000 abstract description 3
- 241000282898 Sus scrofa Species 0.000 description 29
- 239000010865 sewage Substances 0.000 description 8
- 238000012545 processing Methods 0.000 description 7
- 210000003608 fece Anatomy 0.000 description 6
- 230000000694 effects Effects 0.000 description 5
- 238000009434 installation Methods 0.000 description 5
- 238000013461 design Methods 0.000 description 3
- 239000010815 organic waste Substances 0.000 description 3
- 241001465754 Metazoa Species 0.000 description 2
- OAICVXFJPJFONN-UHFFFAOYSA-N Phosphorus Chemical compound [P] OAICVXFJPJFONN-UHFFFAOYSA-N 0.000 description 2
- XKMRRTOUMJRJIA-UHFFFAOYSA-N ammonia nh3 Chemical compound N.N XKMRRTOUMJRJIA-UHFFFAOYSA-N 0.000 description 2
- 238000005842 biochemical reaction Methods 0.000 description 2
- 210000005056 cell body Anatomy 0.000 description 2
- 230000007812 deficiency Effects 0.000 description 2
- 230000018044 dehydration Effects 0.000 description 2
- 238000006297 dehydration reaction Methods 0.000 description 2
- 239000003337 fertilizer Substances 0.000 description 2
- 230000005484 gravity Effects 0.000 description 2
- 230000003301 hydrolyzing effect Effects 0.000 description 2
- 238000007689 inspection Methods 0.000 description 2
- 239000010871 livestock manure Substances 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 2
- 229910052698 phosphorus Inorganic materials 0.000 description 2
- 239000011574 phosphorus Substances 0.000 description 2
- 230000000717 retained effect Effects 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- 241000894006 Bacteria Species 0.000 description 1
- 229910000975 Carbon steel Inorganic materials 0.000 description 1
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 1
- 229910000831 Steel Inorganic materials 0.000 description 1
- 241000216843 Ursus arctos horribilis Species 0.000 description 1
- 230000000844 anti-bacterial effect Effects 0.000 description 1
- 229940088710 antibiotic agent Drugs 0.000 description 1
- 238000006065 biodegradation reaction Methods 0.000 description 1
- 239000010962 carbon steel Substances 0.000 description 1
- 239000003610 charcoal Substances 0.000 description 1
- 238000011109 contamination Methods 0.000 description 1
- 239000013078 crystal Substances 0.000 description 1
- 239000000645 desinfectant Substances 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 238000009826 distribution Methods 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000003344 environmental pollutant Substances 0.000 description 1
- 238000001125 extrusion Methods 0.000 description 1
- 230000009123 feedback regulation Effects 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- 239000011521 glass Substances 0.000 description 1
- 230000009931 harmful effect Effects 0.000 description 1
- 239000001257 hydrogen Substances 0.000 description 1
- 229910052739 hydrogen Inorganic materials 0.000 description 1
- 230000007774 longterm Effects 0.000 description 1
- 229920002521 macromolecule Polymers 0.000 description 1
- 230000002503 metabolic effect Effects 0.000 description 1
- 244000005700 microbiome Species 0.000 description 1
- 238000006396 nitration reaction Methods 0.000 description 1
- 235000016709 nutrition Nutrition 0.000 description 1
- 239000005416 organic matter Substances 0.000 description 1
- 238000012946 outsourcing Methods 0.000 description 1
- 238000012856 packing Methods 0.000 description 1
- 239000002574 poison Substances 0.000 description 1
- 231100000614 poison Toxicity 0.000 description 1
- 231100000719 pollutant Toxicity 0.000 description 1
- FGIUAXJPYTZDNR-UHFFFAOYSA-N potassium nitrate Chemical compound [K+].[O-][N+]([O-])=O FGIUAXJPYTZDNR-UHFFFAOYSA-N 0.000 description 1
- 230000002035 prolonged effect Effects 0.000 description 1
- 238000005086 pumping Methods 0.000 description 1
- 239000002689 soil Substances 0.000 description 1
- 238000005476 soldering Methods 0.000 description 1
- 239000010935 stainless steel Substances 0.000 description 1
- 229910001220 stainless steel Inorganic materials 0.000 description 1
- 239000010959 steel Substances 0.000 description 1
- 239000006228 supernatant Substances 0.000 description 1
- 210000004243 sweat Anatomy 0.000 description 1
- 238000003466 welding Methods 0.000 description 1
Classifications
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W10/00—Technologies for wastewater treatment
- Y02W10/30—Wastewater or sewage treatment systems using renewable energies
- Y02W10/33—Wastewater or sewage treatment systems using renewable energies using wind energy
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W10/00—Technologies for wastewater treatment
- Y02W10/30—Wastewater or sewage treatment systems using renewable energies
- Y02W10/37—Wastewater or sewage treatment systems using renewable energies using solar energy
Landscapes
- Purification Treatments By Anaerobic Or Anaerobic And Aerobic Bacteria Or Animals (AREA)
Abstract
The utility model relates to a waste water integrated treating equipment raises pigs belongs to effluent treatment plant technical field. This waste water integrated treating equipment raises pigs includes solid -liquid separation equipment, anaerobic reaction device, the equalizing basin, first elevator pump, hydrolysis -acidification pool, pack, the oxygen deficiency pond, the air -blower, first aeration pipe, the sludge impoundment, the sludge pump, the good oxygen pond of MBR, second aeration pipe, produce the water water intaking valve, wash the outlet valve, produce the water pump, produce the water outlet valve, the backwash water intaking valve, the water intaking valve is washed to the medicine, pressure switch, the clean water basin, the disinfection pond, third aeration pipe and delivery port, this waste water treatment equipment structure is retrencied, each part sets up rationally, equipment cost has effectively been practiced thrift, the quality of water of not only handling reaches emission standard completely, the waste water of still will raising pigs turns into new forms of energy and recycles.
Description
Technical field
This utility model belongs to wastewater treatment equipment technical field and in particular to a kind of Pig raising wastewater is close-coupled processing sets
Standby.
Background technology
The development of pig industry not only provides the carnivorous source of a large amount of high-quality for people, also improves the life product of people
Matter.
But a large amount of organic wastes can be produced during Swine Production, in these organic wastes, contain substantial amounts of life
Material energy and organic manure resource, directly discharged if do not processed and comprehensively utilized, not only severe contamination water source and ecology
Natural environment, also can have a negative impact to production, additionally, the significant wastage of resource also can be caused.If at Pig raising wastewater
Reason is improper, and liquid dung overflows, and can produce great harmful effect to environment.China's existing Pig raising wastewater processing equipment is numerous at present
Many, but the deficiency due to device structure design, lead to the excellent equipment of actual processing effect few, simultaneously as at great majority
The somewhat expensive of reason equipment, leads to the input of wastewater treatment to be far longer than output, hinders its popularization and application.
Therefore a kind of equipment investment is few, and Pig raising wastewater processes that output is high, and the raising pigs of recoverable Pig raising wastewater resource
Waste water integrated equipment for wastewater treatment is just particularly important.
Content of the invention
The purpose of this utility model is to overcome the deficiencies in the prior art and provides a kind of Pig raising wastewater integrated equipment for wastewater treatment,
This sewage treatment equipment structure is simplified, and each part setting rationally, is effectively saved cost of equipment, the water quality not only processing reaches completely
To discharge standard, also Pig raising wastewater is converted into new forms of energy and recycles.
Pig raising wastewater integrated equipment for wastewater treatment, including equipment for separating liquid from solid, anaerobic reaction device, regulating reservoir, the first lifting
Pump, hydrolysis acidification pool, filler, anoxic pond, aerator, the first aeration tube, sludge-tank, sludge pump, MBR Aerobic Pond, the second aeration
Pipe, produce water water intaking valve, cleaning outlet valve, produce water pump, produce water outlet valve, water intaking valve washed by backwash water intaking valve, medicine, pressure switch, clear
Pond, sterilization pool, the 3rd aeration tube and outlet, wherein said equipment for separating liquid from solid, anaerobic reaction device, regulating reservoir, first
Elevator pump and hydrolysis acidification pool pass sequentially through pipeline and connect, and the entrance of described first elevator pump connects regulating reservoir bottom by pipeline
Portion, the outlet of the first elevator pump connects hydrolysis acidification pool top by pipeline, is provided with filler, described water in described hydrolysis acidification pool
Solution acidification pool, anoxic pond, sludge-tank, MBR Aerobic Pond, clear water reserviors and sterilization pool adjacent connect setting successively, wherein said anoxia
It is provided with the first aeration tube in pond, in MBR Aerobic Pond, is provided with the second aeration tube, in sterilization pool, be provided with the 3rd aeration tube, described air blast
Machine, the first aeration tube, the second aeration tube and the 3rd aeration tube pass sequentially through pipeline and connect, described aerator, the first aeration tube, the
The connecting line of two aeration tubes and the 3rd aeration tube passes sequentially through anoxic pond, sludge-tank, MBR Aerobic Pond and clear water reserviors from aerator
Connect to the 3rd aeration tube, the entrance of described sludge pump connects sludge-tank and MBR Aerobic Pond respectively by pipeline, the going out of sludge pump
Mouth mouth connects sludge-tank and MBR Aerobic Pond respectively by pipeline, is provided with MBR membrane bioreactor in described MBR Aerobic Pond, described
Produce water water intaking valve, one end of cleaning outlet valve is all passed through pipeline and MBR membrane bioreactor and connected, described product water water intaking valve another
One end successively with pressure switch, produce water pump, produce water outlet valve be connected to clear water reserviors by pipeline, described product water water intaking valve another
End is connected to clear water reserviors by pipeline with backwash water intaking valve, and the other end of described product water water intaking valve passes through pipeline with backwash water intaking valve
Connect to sterilization pool, the other end of described cleaning outlet valve is sequentially connected product water pump, pressure switch by pipeline and produces water water inlet
The other end of valve simultaneously forms closed-loop path, and the side wall of described sterilization pool is provided with outlet.
Further, described Pig raising wastewater integrated equipment for wastewater treatment, wherein said equipment for separating liquid from solid divides for solid-liquid
Disembark.
Further, described Pig raising wastewater integrated equipment for wastewater treatment, wherein said anaerobic reaction device is up-flow
Anaerobic mud bed.
Further, described Pig raising wastewater integrated equipment for wastewater treatment, is provided with the first liquid level in wherein said regulating reservoir
Switch, is provided with grid in described regulating reservoir, and described grille strip gap length is less than 10mm.
Further, described Pig raising wastewater integrated equipment for wastewater treatment, wherein said MBR Aerobic Pond top is provided with second
Liquid-level switch.
Further, described Pig raising wastewater integrated equipment for wastewater treatment, middle part in wherein said hydrolysis acidification pool
It is provided with filler.
Further, described Pig raising wastewater integrated equipment for wastewater treatment, is provided with activity in wherein said MBR Aerobic Pond
Charcoal.
Further, above-mentioned Pig raising wastewater integrated equipment for wastewater treatment, wherein said hydrolysis acidification pool, anoxic pond, MBR
It is equipped with the second outlet, sludge-tank is provided with overfall on the side wall of Aerobic Pond and clear water reserviors.
This practicality compared with prior art, has the advantages that：
First：Pig raising wastewater integrated equipment for wastewater treatment structure of the present utility model is simplified, and each part setting rationally, effectively saves
About cost of equipment, the water quality not only processing is fully achieved discharge standard, also Pig raising wastewater is converted into new forms of energy and recycles；
Second：Pig raising wastewater integrated equipment for wastewater treatment of the present utility model stablizes easy care, has automatically and manually two kinds
Control mode, save energy to greatest extent, and the overflow of sewage is arranged on prime as far as possible；
3rd：Pig raising wastewater integrated equipment for wastewater treatment of the present utility model follows unpowered principle, can make full use of physical features
Difference, hydraulic gravity gravity flow effect, and no medicine system, main energy consuming part is aerator aeration power consumption and film suction pump, backwash
Pump power consumption.As needed, also can be selected for wind energy, solar power system, realize " zero power consumption "；
4th：The close-coupled processing compact conformation of Pig raising wastewater of the present utility model, floor space are little, small investment, installation side
Just, be conducive to managing concentratedly.And electrical equipment, the mechanical life of equipment because it reasonably designs, can be greatly prolonged.In addition this sets
Standby control system is multiple functional, and equipment has a manual, automatic maneuverability pattern, achievable pond high-low water alarm, automatic detecting,
The function such as patrol and examine manually, and there is self-inspection, failure protection function and extremely strong capacity of resisting disturbance.
Brief description
Fig. 1 be this utility model Pig raising wastewater integrated equipment for wastewater treatment structural representation, wherein, 1, solid-liquid separation dress
Put；2nd, anaerobic reaction device；3rd, regulating reservoir；31st, the first liquid-level switch；4th, the first elevator pump；5th, hydrolysis acidification pool；51st, filler；
6th, anoxic pond；61st, aerator；62nd, the first aeration tube；7th, sludge-tank；71st, sludge pump；8th, MBR Aerobic Pond；81st, the second aeration
Pipe；82nd, produce water water intaking valve；83rd, clean outlet valve；84th, produce water pump；85th, produce water outlet valve；86th, backwash water intaking valve；87th, medicine is washed
Water intaking valve；88th, the second liquid-level switch；89th, pressure switch；9th, clear water reserviors；10th, sterilization pool；101st, the 3rd aeration tube；102nd, water outlet
Mouthful.
Specific embodiment
Below by specific embodiment, this practicality is described in further detail, but those skilled in the art will manage
Solution, the following example is merely to illustrate this utility model, and should not be regarded as limiting scope of the present utility model.
Embodiment
As shown in figure 1, Pig raising wastewater integrated equipment for wastewater treatment, including equipment for separating liquid from solid 1, anaerobic reaction device 2, adjust
Pond 3, the first elevator pump 4, hydrolysis acidification pool 5, filler 51, anoxic pond 6, aerator 61, the first aeration tube 62, sludge-tank 7, mud
Pump 71, MBR Aerobic Pond 8, the second aeration tube 81, produce water water intaking valve 82, cleaning outlet valve 83, produce water pump 84, produce water outlet valve 85,
Backwash water intaking valve 86, medicine wash water intaking valve 87, pressure switch 89, clear water reserviors 9, sterilization pool 10, the 3rd aeration tube 101 and outlet
102, wherein said equipment for separating liquid from solid 1, anaerobic reaction device 2, regulating reservoir 3, the first elevator pump 4 and hydrolysis acidification pool 5 are successively
Connected by pipeline, the entrance of described first elevator pump 4 connects regulating reservoir 3 bottom by pipeline, and the outlet of the first elevator pump 4 is led to
Cross pipeline and connect hydrolysis acidification pool 5 top, in described hydrolysis acidification pool 5, be provided with filler 51, described hydrolysis acidification pool 5, anoxic pond
6th, sludge-tank 7, MBR Aerobic Pond 8, clear water reserviors 9 and sterilization pool 10 adjacent connect setting successively, is provided with wherein said anoxic pond 6
First aeration tube 62, is provided with the second aeration tube 81 in MBR Aerobic Pond 8, be provided with the 3rd aeration tube 101, described drum in sterilization pool 10
Blower fan 61, the first aeration tube 62, the second aeration tube 81 and the 3rd aeration tube 101 pass sequentially through pipeline and connect, described aerator 61,
The connecting line of the first aeration tube 62, the second aeration tube 81 and the 3rd aeration tube 101 from aerator 61 pass sequentially through anoxic pond 6,
Sludge-tank 7, MBR Aerobic Pond 8 and clear water reserviors 9 connect to the 3rd aeration tube 101, and the entrance of described sludge pump 71 is by pipeline respectively
Connect sludge-tank 7 and MBR Aerobic Pond 8, the outlet mouth of sludge pump 71 connects sludge-tank 7 and MBR Aerobic Pond 8 respectively by pipeline,
It is provided with MBR membrane bioreactor, described product water water intaking valve 82, one end of cleaning outlet valve 83 are all passed through in described MBR Aerobic Pond 8
Pipeline and MBR membrane bioreactor connect, the described other end producing water water intaking valve 82 successively with pressure switch 89, produce water pump 84,
Produce water outlet valve 85 to connect to clear water reserviors 9 by pipeline, the described other end producing water water intaking valve 82 is passed through with backwash water intaking valve 86
Pipeline connects to clear water reserviors 9, and the described other end producing water water intaking valve 82 is connected to sterilization pool by pipeline with backwash water intaking valve 86
10, the other end of described cleaning outlet valve 83 is sequentially connected product water pump 84, pressure switch 89 by pipeline and produces water water intaking valve 82
The other end and form closed-loop path, the side wall of described sterilization pool 10 is provided with outlet 102.
Equipment for separating liquid from solid 1 used in this utility model can be solid-liquid separating machine, and anaerobic reaction device 2 can be up-flow
Anaerobic mud bed, it is provided with the first liquid-level switch 31 in described regulating reservoir 3, and be provided with grid in described regulating reservoir 3, described grid
Bar gap length is less than 10mm, and when arranging thickness twice grid, coarse rack bar gap length is 10～20mm, and fine fack bar is empty
Gap width is 2.0mm.It is provided with the second liquid-level switch 88 at described MBR Aerobic Pond 8 top, middle in described hydrolysis acidification pool 5
Position is provided with filler 51, is provided with activated carbon in described MBR Aerobic Pond 8, aerobic in described hydrolysis acidification pool 5, anoxic pond 6, MBR
Second outlet is equipped with the side wall of pond 8 and clear water reserviors 9, sludge-tank 7 is provided with overfall.
Wherein, solid-liquid separating machine is used for the processed of plant's fowl and animal excrement, can be by various fowl and animal excrements through extruding
After dehydration, being lowered into the solid-state feces concentration of upflow anaerobic sludge blanket process, thus improve biogas efficiency, avoiding long-term simultaneously
Operation leads to upflow anaerobic sludge blanket process to block, extension reactor service life.
Solid-liquid separating machine principle enters main frame for liquid dung, is pushed in front of main frame through extrusion spiral auger by liquid dung, main frame
Front pressure constantly increases, and just pushes discharge port open, reach the purpose of extruding and discharging to setup pressure value.Solid manure can be made
Agricultural fertilizer is used.
Anaerobic reaction device is mainly used to carry out anaerobic bio-treated, using the metabolic characteristic of anerobe, not
Under conditions of external source energy need to be provided, to be reduced Organic substance as hydrogen acceptor, there is the methane gas of energy value simultaneously.
Anaerobic biotreatment method is applicable not only to high concentrated organic wastewater, and water inlet BOD maximum concentration, up to tens thousand of mg/l, is equally applicable to
Low-concentration organic waste water, such as municipal sewage etc..
Anaerobic bio-treated process energy consumption is low；Organic volumetric loading is high, generally 5-10kgCOD/m3.d, highest up to
30-50kgCOD/m3.d；Surplus sludge volume is few；Anaerobe is low to nutritional need, resistance to poison strong, the organic matter molecular mass of degradable
High；Anti impulsion load ability is strong；The biogas of output is a kind of clean energy resource.
Anaerobic reaction device adopts upflow anaerobic sludge blanket process, and this anaerobic reaction device is fitted for different solid content sewage
Ying Xingqiang, and its structure, operation oam are relatively easy, cost is relatively low.
Pig raising wastewater after solid-liquid separating machine processed enters upflow anaerobic sludge blanket process, through up-flow anaerobic sludge
After bed anaerobic treatment, COD clearance is up to 75%-85%.
Grid setting is as follows：When arranging one grid, grille strip gap length should be less than 10mm；Setting thickness twice grid
When, coarse rack bar gap length is 10～20mm, and fine fack bar gap length is 2.0mm.During using one planar grille, manually
Periodically remove debris.Grid spacing 2mm, grizzly bar is stainless steel, and grid is placed in frame trough, is prevented with carbon steel welding liner
Corruption, frame trough size 1600 × 1200 × 1200mm.After grid regulating reservoir, waste water is pumped to hydrolysis acidification pool by elevator pump.
Waste water enters in hydrolysis acidification pool, and hydrolysis acidification pool carries out water distribution by water distributor, and waste water is given birth in hydrolytic tank filler
Fully mixed, contacted, being adsorbed, being decomposed with anaerobic mud bed on thing film, macromolecule organic is carried out being degraded to low molecule
Organic substance, raising can biochemical effects.The discharge by anaerobic sludge for the pollutant absorbing, enters sludge system.Typically foster
Pig waste water time of staying in hydrolysis acidification pool is 4 hours, and that is, hydrolytic tank dischargeable capacity is 30m3, available depth is 3.2m, interior
Add semi soft packing.
Because waste water contains the ammonia nitrogen of a large amount, phosphorus, affect the activity of follow-up aerobe, therefore set anoxic pond and carry out denitrogenation and remove
Phosphorus.Pig raising wastewater time of staying in anoxic pond is 2.5 hours, and that is, anoxic pond dischargeable capacity is 19m3, available depth is 3.2m.
The sewage processing through anoxic pond, enters in MBR Aerobic Pond, using film in biochemical reaction tank containing dirt
Water is filtered, and realizes mud-water separation.On the one hand, film has retained the microorganism in reaction tank, makes the activated sludge concentration in pond
Big increase, reaches very high level, so that the biochemical reaction of degraded sewage is proceeded more quickly more thorough, on the other hand, due to film
High filtering precision it is ensured that water outlet is as clear as crystal, obtain high-quality product water.
Membrane cisterna setting MBR membrane bioreactor and supporting water outlet, backwash, medicine are washed, aeration etc..Aeration in MBR film area
Have two purposes, one be for membrane module around air water vibration, keep film surface cleaning, two is to provide required for biodegradation
Oxygen.By the efficient crown_interception of film, whole antibacterials and float are all dammed in Aeration tank, can be with effectively catching nitre
Change bacterium, so that nitration reaction is smoothed out, effectively remove ammonia nitrogen；The larger molecular organicses being difficult to degrade can be retained simultaneously, extend
Its time of staying in the reactor, it is allowed to be degraded to greatest extent.It is regular that excess sludge passes through film area residual sludge pump
Discharge, the concentration of activated sludge and sludge age in controllable device.Pig raising wastewater time of staying in MBR Aerobic Pond is 8 hours,
I.e. aerobic/MBR membrane cisterna dischargeable capacity is 60m3, available depth is 3.2m.Aeration rate presses MBR film institute air demand gas-water ratio 30:1 meter
Calculate, aeration rate is 3.75m3/min.Aerator aeration rate is taken to be 3.95m3/min.
MBR Aerobic Pond water outlet is by being pumped to after clear water reserviors entrance sterilization pool.Sterilization pool adds water outlet row after disinfectant sterilization
To sewage network.By the regular auto-pumping of sludge pump to sludge-tank, sludge-tank sets overfall, supernatant to MBR Aerobic Pond pool bottom sludge
Liquid flow to anoxic pond certainly.In sludge-tank, mud drains into solid-liquid separating machine dehydration, can be used as agricultural fertilizer.
Cell body in this utility model equipment can be welded using glass steel material, wherein hydrolysis acidification pool, anoxic pond, good
Oxygen/MBR membrane cisterna, clear water reserviors, sterilization pool, sludge-tank can be according to parameter settings shown in table 1 below：
The each cell body arrange parameter table of table 1
In actual installation, according to " rational deployment, technological process is orderly, characteristics of compact layout, reduces and takes up an area, and function is divided as far as possible
Area rationally, not only improves and produces again convenient management " station area planar design principle, simultaneously take account of the nature bar such as landform, landforms
Part, in conjunction with Inlet and outlet water direction, the many factors such as factory-out road and direction of building.All of soil pipe, sludge pipe is PVC
Pressure-resistant pipeline, mud valve is butterfly valve, and manually-operated gate is gate valve or butterfly valve；The installation of various equipment should be promulgated according to country
Carry out about specification and code.Sweat soldering or flange is adopted to connect between pipeline；In the place that pipeline is intensive, pipeline valve
The direction of position and method door handle should be arranged on the position being easy to operate；Pipeline valve in sewage disposal main body structures should be use up
It is possibly mounted at by inspection shaft, in order to opening and adjusting；The installation of various equipment should according to country promulgate relevant specification and
Code is carried out, and the wherein installation of outsourcing device need to be carried out by corresponding product description.
In this utility model, the big equipment of power consumption is mainly water pump, aerator, on-stream makes pump operating point position
In efficiency highest region, to save power consumption.In elevation arrangement, save the loss of flood peak, reduce jump water height, to save water pump lifting
Highly, save power consumption.From effective control instrument, flow of inlet water and correlation water data etc. are carried out and automatically monitors, pass through
Optimal Control is realized in signal feedback regulation, and Reasonable adjustment operating mode is it is ensured that efficient operation.
Claims (8)
1. Pig raising wastewater integrated equipment for wastewater treatment is it is characterised in that include equipment for separating liquid from solid（1）, anaerobic reaction device（2）、
Regulating reservoir（3）, the first elevator pump（4）, hydrolysis acidification pool（5）, filler（51）, anoxic pond（6）, aerator（61）, the first aeration
Pipe（62）, sludge-tank（7）, sludge pump（71）, MBR Aerobic Pond（8）, the second aeration tube（81）, produce water water intaking valve（82）, wash out
Water valve（83）, produce water pump（84）, produce water outlet valve（85）, backwash water intaking valve（86）, medicine wash water intaking valve（87）, pressure switch
（89）, clear water reserviors（9）, sterilization pool（10）, the 3rd aeration tube（101）And outlet（102）, wherein said equipment for separating liquid from solid
（1）, anaerobic reaction device（2）, regulating reservoir（3）, the first elevator pump（4）And hydrolysis acidification pool（5）Pass sequentially through pipeline to connect, institute
State the first elevator pump（4）Entrance regulating reservoir is connected by pipeline（3）Bottom, the first elevator pump（4）Outlet by pipeline even
Connect hydrolysis acidification pool（5）Top, described hydrolysis acidification pool（5）Inside it is provided with filler（51）, described hydrolysis acidification pool（5）, anoxic pond
（6）, sludge-tank（7）, MBR Aerobic Pond（8）, clear water reserviors（9）And sterilization pool（10）Adjacent connect setting successively, wherein said anoxia
Pond（6）Inside it is provided with the first aeration tube（62）, MBR Aerobic Pond（8）Inside it is provided with the second aeration tube（81）, sterilization pool（10）Inside it is provided with
Three aeration tubes（101）, described aerator（61）, the first aeration tube（62）, the second aeration tube（81）With the 3rd aeration tube（101）According to
Secondary connected by pipeline, described aerator（61）, the first aeration tube（62）, the second aeration tube（81）With the 3rd aeration tube（101）
Connecting line from aerator（61）Pass sequentially through anoxic pond（6）, sludge-tank（7）, MBR Aerobic Pond（8）And clear water reserviors（9）Connect
To the 3rd aeration tube（101）, described sludge pump（71）Entrance sludge-tank is connected respectively by pipeline（7）With MBR Aerobic Pond
（8）, sludge pump（71）Outlet sludge-tank is connected respectively by pipeline（7）With MBR Aerobic Pond（8）, described MBR Aerobic Pond（8）
Inside it is provided with MBR membrane bioreactor, described product water water intaking valve（82）, cleaning outlet valve（83）One end all by pipeline and MBR
Membrane bioreactor connects, described product water water intaking valve（82）The other end successively with pressure switch（89）, produce water pump（84）, produce water
Outlet valve（85）Connected to clear water reserviors by pipeline（9）, described product water water intaking valve（82）The other end and backwash water intaking valve（86）
Connected to clear water reserviors by pipeline（9）, described product water water intaking valve（82）The other end and backwash water intaking valve（86）By pipeline even
It is connected to sterilization pool（10）, described cleaning outlet valve（83）The other end product water pump is sequentially connected by pipeline（84）, pressure switch
（89）With product water water intaking valve（82）The other end and form closed-loop path, described sterilization pool（10）Side wall be provided with outlet
（102）.
2. Pig raising wastewater integrated equipment for wastewater treatment according to claim 1 is it is characterised in that described equipment for separating liquid from solid
（1）For solid-liquid separating machine.
3. Pig raising wastewater integrated equipment for wastewater treatment according to claim 1 is it is characterised in that described anaerobic reaction device
（2）For upflow anaerobic sludge blanket process.
4. Pig raising wastewater integrated equipment for wastewater treatment according to claim 1 is it is characterised in that described regulating reservoir（3）Inside set
There is the first liquid-level switch（31）, described regulating reservoir（3）Inside it is provided with grid, described grille strip gap length is less than 10mm.
5. Pig raising wastewater integrated equipment for wastewater treatment according to claim 1 is it is characterised in that described MBR Aerobic Pond（8）Top
Portion is provided with the second liquid-level switch（88）.
6. Pig raising wastewater integrated equipment for wastewater treatment according to claim 1 is it is characterised in that described hydrolysis acidification pool（5）
Interior middle part is provided with filler（51）.
7. Pig raising wastewater integrated equipment for wastewater treatment according to claim 1 is it is characterised in that described MBR Aerobic Pond（8）Interior
It is provided with activated carbon.
8. the Pig raising wastewater integrated equipment for wastewater treatment according to any one of claim 1 to 7 is it is characterised in that described hydrolysis
Acidification pool（5）, anoxic pond（6）, MBR Aerobic Pond（8）And clear water reserviors（9）Side wall on be equipped with the second outlet, sludge-tank（7）
It is provided with overfall.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620932930.5U CN205974187U (en) | 2016-08-25 | 2016-08-25 | Waste water integrated treating equipment raises pigs |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620932930.5U CN205974187U (en) | 2016-08-25 | 2016-08-25 | Waste water integrated treating equipment raises pigs |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205974187U true CN205974187U (en) | 2017-02-22 |
Family
ID=58033564
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201620932930.5U Expired - Fee Related CN205974187U (en) | 2016-08-25 | 2016-08-25 | Waste water integrated treating equipment raises pigs |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN205974187U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107200431A (en) * | 2017-05-31 | 2017-09-26 | 广东维清环境工程有限公司 | A kind of Pig raising wastewater deep treatment method |
| CN107235613A (en) * | 2017-08-14 | 2017-10-10 | 韩保洋 | A kind of compact simplified sewage disposal MBR film bioreactor devices |
-
2016
- 2016-08-25 CN CN201620932930.5U patent/CN205974187U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107200431A (en) * | 2017-05-31 | 2017-09-26 | 广东维清环境工程有限公司 | A kind of Pig raising wastewater deep treatment method |
| CN107235613A (en) * | 2017-08-14 | 2017-10-10 | 韩保洋 | A kind of compact simplified sewage disposal MBR film bioreactor devices |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN104843954B (en) | Sewage treatment device and treatment method thereof for large-scale sewage treatment station | |
| CN101863587B (en) | Process for purifying and recycling biomass organic wastewater | |
| CN103274571B (en) | Resource utilization and treatment method of livestock breeding wastewater | |
| CN103304101B (en) | Resource utilization and regeneration circulation utilization device for livestock and poultry breeding wastewater | |
| CN103288303A (en) | Livestock/poultry breeding wastewater resource utilization and regeneration recycling method | |
| CN101759323A (en) | Treatment combined process for pig farm waste water with high nitrogen content | |
| CN101817615A (en) | Anaerobic-sequencing batch biofilm reactor-artificial wetland method for treating piggery wastewater | |
| CN107265802A (en) | The treatment for cow manure system and processing method of a kind of dairy cow farm | |
| CN101157501B (en) | Helminth attaching biological bed for deweighting city sewage sludge | |
| CN205635292U (en) | Sewage treatment ware is used at rural family | |
| CN103288302B (en) | Livestock/poultry breeding wastewater resource utilization and treatment device | |
| CN103848535B (en) | Multimedium renewable biological filtering method and device | |
| CN104692590A (en) | Sewage treatment system | |
| CN205974187U (en) | Waste water integrated treating equipment raises pigs | |
| CN105036819A (en) | Facility for producing earthworm breeding loam by utilizing aquaculture sewage and method | |
| CN104478099B (en) | Detachable sewage treatment equipment | |
| CN110790455A (en) | Integrated sewage treatment equipment and sewage treatment method | |
| CN203333441U (en) | Resource utilization and treatment device of livestock and poultry breeding waste water | |
| CN206940693U (en) | A kind of mobile integrated sewage disposal device of suitable the Yellow River camp buildings | |
| CN210481156U (en) | Rural sewage treatment device in integration river course | |
| CN204752476U (en) | Sewage treatment device at large -scale sewage treatment station | |
| CN204874219U (en) | Handle rural domestic sewage's biological ecological composite set | |
| CN207619210U (en) | A kind of energy-saving and emission-reducing urban wastewater treatment equipment | |
| CN208087407U (en) | A kind of brominated organic wastewater treating system | |
| CN205616729U (en) | Sewage treatment system |
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: 20170222 |