CN106927636A - A kind of ecological environment protection toilet processing unit - Google Patents
A kind of ecological environment protection toilet processing unit Download PDFInfo
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- CN106927636A CN106927636A CN201710238214.6A CN201710238214A CN106927636A CN 106927636 A CN106927636 A CN 106927636A CN 201710238214 A CN201710238214 A CN 201710238214A CN 106927636 A CN106927636 A CN 106927636A
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- water tank
- activated carbon
- fluidized bed
- water
- ozone
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- 238000012545 processing Methods 0.000 title claims abstract description 13
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 139
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims abstract description 77
- CBENFWSGALASAD-UHFFFAOYSA-N Ozone Chemical compound [O-][O+]=O CBENFWSGALASAD-UHFFFAOYSA-N 0.000 claims abstract description 50
- 230000001105 regulatory effect Effects 0.000 claims abstract description 31
- 239000006228 supernatant Substances 0.000 claims abstract description 24
- 238000005273 aeration Methods 0.000 claims description 21
- 238000012856 packing Methods 0.000 claims description 12
- 239000003610 charcoal Substances 0.000 claims description 11
- 239000000463 material Substances 0.000 claims description 10
- 230000000694 effects Effects 0.000 claims description 9
- 230000029087 digestion Effects 0.000 claims description 6
- 238000001179 sorption measurement Methods 0.000 claims description 6
- 239000004744 fabric Substances 0.000 claims description 4
- 239000006004 Quartz sand Substances 0.000 claims description 3
- 239000002699 waste material Substances 0.000 claims description 3
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 claims description 2
- 239000010865 sewage Substances 0.000 abstract description 18
- 238000000034 method Methods 0.000 abstract description 11
- 239000010802 sludge Substances 0.000 abstract description 8
- 238000001914 filtration Methods 0.000 abstract description 6
- 238000004659 sterilization and disinfection Methods 0.000 abstract description 5
- 239000002351 wastewater Substances 0.000 abstract description 4
- 239000003814 drug Substances 0.000 abstract description 3
- 230000015572 biosynthetic process Effects 0.000 abstract description 2
- 229910052799 carbon Inorganic materials 0.000 abstract description 2
- 230000010354 integration Effects 0.000 abstract description 2
- 230000009965 odorless effect Effects 0.000 abstract description 2
- 241000894006 Bacteria Species 0.000 description 5
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 5
- 238000011001 backwashing Methods 0.000 description 5
- 239000012530 fluid Substances 0.000 description 5
- 239000007789 gas Substances 0.000 description 5
- 239000001301 oxygen Substances 0.000 description 5
- 229910052760 oxygen Inorganic materials 0.000 description 5
- 244000005700 microbiome Species 0.000 description 4
- 238000010521 absorption reaction Methods 0.000 description 3
- 206010059410 Faecaluria Diseases 0.000 description 2
- 238000004134 energy conservation Methods 0.000 description 2
- 230000007613 environmental effect Effects 0.000 description 2
- 210000003608 fece Anatomy 0.000 description 2
- 238000007667 floating Methods 0.000 description 2
- 238000005243 fluidization Methods 0.000 description 2
- 238000012423 maintenance Methods 0.000 description 2
- 238000006213 oxygenation reaction Methods 0.000 description 2
- 239000007790 solid phase Substances 0.000 description 2
- 230000001954 sterilising effect Effects 0.000 description 2
- 206010002660 Anoxia Diseases 0.000 description 1
- 241000976983 Anoxia Species 0.000 description 1
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 1
- 206010021143 Hypoxia Diseases 0.000 description 1
- 229910002651 NO3 Inorganic materials 0.000 description 1
- NHNBFGGVMKEFGY-UHFFFAOYSA-N Nitrate Chemical compound [O-][N+]([O-])=O NHNBFGGVMKEFGY-UHFFFAOYSA-N 0.000 description 1
- RTAQQCXQSZGOHL-UHFFFAOYSA-N Titanium Chemical compound [Ti] RTAQQCXQSZGOHL-UHFFFAOYSA-N 0.000 description 1
- UCTAMTCGWMMARC-UHFFFAOYSA-N [O-][N+]([O-])=O.[O-][N+]([O-])=O.[O-][N+]([O-])=O.N.[NH6+3] Chemical compound [O-][N+]([O-])=O.[O-][N+]([O-])=O.[O-][N+]([O-])=O.N.[NH6+3] UCTAMTCGWMMARC-UHFFFAOYSA-N 0.000 description 1
- 230000007953 anoxia Effects 0.000 description 1
- 230000001580 bacterial effect Effects 0.000 description 1
- 230000015556 catabolic process Effects 0.000 description 1
- 238000006731 degradation reaction Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 230000005611 electricity Effects 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
- 238000001704 evaporation Methods 0.000 description 1
- 230000008020 evaporation Effects 0.000 description 1
- 239000000945 filler Substances 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 230000002906 microbiologic effect Effects 0.000 description 1
- 238000006396 nitration reaction Methods 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 238000006385 ozonation reaction Methods 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 239000012071 phase Substances 0.000 description 1
- 231100000572 poisoning Toxicity 0.000 description 1
- 230000000607 poisoning effect Effects 0.000 description 1
- 231100000719 pollutant Toxicity 0.000 description 1
- 238000012805 post-processing Methods 0.000 description 1
- 230000001681 protective effect Effects 0.000 description 1
- 238000011002 quantification Methods 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 238000010008 shearing Methods 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 239000002910 solid waste Substances 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
- 239000010902 straw Substances 0.000 description 1
- 239000013589 supplement Substances 0.000 description 1
- 229910052719 titanium Inorganic materials 0.000 description 1
- 239000010936 titanium Substances 0.000 description 1
- 238000012546 transfer Methods 0.000 description 1
- 210000002700 urine Anatomy 0.000 description 1
- 239000003403 water pollutant Substances 0.000 description 1
- 239000002023 wood Substances 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F9/00—Multistage treatment of water, waste water or sewage
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/28—Treatment of water, waste water, or sewage by sorption
- C02F1/283—Treatment of water, waste water, or sewage by sorption using coal, charred products, or inorganic mixtures containing them
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/72—Treatment of water, waste water, or sewage by oxidation
- C02F1/78—Treatment of water, waste water, or sewage by oxidation with ozone
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F3/00—Biological treatment of water, waste water, or sewage
- C02F3/28—Anaerobic digestion processes
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F3/00—Biological treatment of water, waste water, or sewage
- C02F3/30—Aerobic and anaerobic processes
- C02F3/301—Aerobic and anaerobic treatment in the same reactor
Landscapes
- Life Sciences & Earth Sciences (AREA)
- Hydrology & Water Resources (AREA)
- Engineering & Computer Science (AREA)
- Environmental & Geological Engineering (AREA)
- Water Supply & Treatment (AREA)
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Treatment Of Water By Oxidation Or Reduction (AREA)
- Water Treatment By Sorption (AREA)
Abstract
The invention discloses a kind of ecological environment protection toilet processing unit,Including foul water tank,Regulating tank,It is anaerobic fluidized bed,Interior circulation aerobe reactor,Ozone tower,Activated carbon adsorber,Lower filtered water tank and supernatant water tank,By foul water tank,Regulating tank,It is anaerobic fluidized bed,Interior circulation aerobe reactor,Ozone tower,Activated carbon adsorber,Lower filtered water tank,Supernatant water tank is successively connected up and down,Will be anaerobic fluidized bed,Interior circulation aerobe reactor,Ozone,The sewage treatment process such as active carbon purifying are integrated in one,High-concentration sewage is collected,By anaerobism,It is aerobic,Disinfection,Water body is filtered,The reclaimed water up to standard of formation colorless and odorless returns again to flush the toilet and uses,Economized on water in running,Without externally discharged waste water,Sludge,Medicament need not be added,Non-secondary pollution,Treatment water is sterilized by filtering,Meet reuse needs,Floor space is small,Device integration is high.
Description
Technical field
The invention belongs to wastewater reusing device technical field, and in particular to a kind of environment-friendly water-saving, what water body can be recycled
Ecological environment protection toilet processing unit.
Background technology
Bio-toilet is intended to water saving, energy-conservation, by resource, the innoxious and minimizing treatment, main use on the spot of mankind's fecaluria
In the outdoor place without perfect water and electricity supply Yu drainage.Main bio-toilet is broadly divided into anhydrous type and has water at present
Two kinds of type, the method that anhydrous type bio-toilet is used is that excreta entrance is arranged on lavatory collective low system, is using stirring
The biological dispensing to slop and with agricultural crop straw or wood chip etc. as main component of uniting is sufficiently stirred for, and is added
Heat, moisture evaporation is acted on by the biochemical degradation of microorganism aerobic bacterium, by mankind's fecaluria resource, innoxious and subtract on the spot
Quantification treatment, the final dry bio-feritlizer of output.There is water type bio-toilet often to use and use environmental project method, blowdown
After separation of solid and liquid, reuse after treatment harmless treatment is carried out to liguid phase pollutant, solid phase is by outward transport after-treatment of packing.It is anhydrous
Type bio-toilet not water consumption, energy-conservation, but there is a problem of that smell is not good with clean environment.There is water type bio-toilet once to add water,
As supplement recycle-water after by the use of urine process, water saving, treatment power consumption is higher than anhydrous type bio-toilet, there is solid waste and beats
Reason trouble is assured, maintenance is difficult, the not good problem of clean environment, the treatment while backwater seldom carries out disinfection, caused in backwater carefully
Bacterium sum is higher, causes safe and healthy problem.And biological treatment needs the regular hour, when flow of the people breaks out suddenly, greatly
Many bio-toilets cannot be effectively treated in time.Therefore, developing one kind can tackle emergency case, only need to once add
Water, water saving in running, without draining, excreta realizes sludge reduction by anaerobic fluidized bed, it is not necessary to set solid phase dirty
Thing packing apparatus is contaminated, backwater is through the advanced treating ecological environment protection toilet processing unit for utilizing that can be circulated to waste water up to standard
Solve the effective way of this problem.
The content of the invention
It is an object of the invention to provide a kind of compact conformation, it is easy to implement, energy consumption is low, efficient, water saving ecological, environmental protective
Lavatory processing unit.
The object of the present invention is achieved like this, including foul water tank, regulating tank, the aerobic life of anaerobic fluidized bed, interior circulation
Thing reactor, ozone tower, activated carbon adsorber, lower filtered water tank and supernatant water tank, described foul water tank connection closet, described dirt
Water tank is connected to regulating tank top, and regulating tank bottom connects anaerobic fluidized bed bottom by pipeline pump, it is anaerobic fluidized bed on
Portion connection interior circulation aerobe reactor bottom, interior circulation aerobe reactor top connection ozone tower bottom, ozone tower
Top connection activated carbon adsorber top, the lower filtered water tank of activated carbon adsorber bottom connection, lower filtered water tank passes through backwash pump
Connection supernatant water tank, supernatant water tank connects the waste preventer of closet；Described activated carbon adsorber top connection regulating tank；It is described
Interior circulation aerobe reactor bottom connection regulating tank；In described interior circulation aerobe reactor inside is set
Cylinder, inner cylinder bottom tightly sets aeration head, and aeration head is connected by pipeline with air pump, and the outer top of inner cylinder sets biologic packing material；It is described
Ozone tower and charcoal absorption tower bottom micro porous aeration head is set be connected ozone generator, described ozone tower and activated carbon suction
Attached top of tower connects ozone tail gas digestion instrument by pipeline.
The present invention passes through foul water tank, regulating tank, anaerobic fluidized bed, interior circulation aerobe reactor, ozone tower, activity
Charcoal adsorption tower, lower filtered water tank, supernatant water tank are connected up and down successively, by anaerobic fluidized bed, interior circulation aerobe reactor, smelly
The sewage treatment process such as oxygen, active carbon purifying are integrated in one, and high-concentration sewage is collected, by anaerobism, aerobic, sterilization
Sterilized, water body is filtered, and the reclaimed water up to standard of formation colorless and odorless returns again to flush the toilet and uses；And activated carbon adsorber top with it is interior
Circulation aerobe reactor bottom all connects regulating tank, and the process starting point that part dirt is sent back to that can will be unable to process is carried out
Circular treatment, improves treatment quality again；Interior circulation aerobe reactor sets inner cylinder, and inner cylinder bottom tightly sets aeration head, exposes
Gas head is connected by pipeline with air air pump, and bucket internal upper part sets biologic packing material, and in inner cylinder aeration process, bubble floating drives
The sewage of bottom is run up, and aerobic zone is formed in inner cylinder, and the water (flow) direction of outer barrel is from top to bottom, barrel-shaped into anoxic zone outside,
Inner/outer tube current are formed and circulated, the biologic packing material that bucket internal upper part is set, and, by oxygenation repeatedly, bubble and microorganism cenobium be not by for sewage
Disconnected shearing refinement, and fine and close tiny floccule body is formed, in aerobic zone, organic pollution is decomposed by microbiological oxidation, while sewage
In ammonia nitrogen nitrate is converted into by the nitrification of microorganism, carry out anti-nitration reaction in anoxic zone, denitrifying bacteria exists
Under anoxia condition, nitrate is reduced, discharges molecular nitrogen (N2), activated sludge gradually sinks to reactor bottom, and upper water becomes clear,
Carried out disinfection into ozone tower, activated carbon adsorber is entered afterwards and is filtered；Biological treatment needs the regular hour, and regulating tank
Setting can then play a part of buffer when flow of the people increases suddenly；The setting of ozone tail gas digestion instrument can then be remained
Remaining ozone decomposed is outer row after oxygen, and nearby oxygen is sufficient for device in running, reduces stink and unplessantness displeasure.Structure of the present invention
It is compact, during whole handling process combined in into a device, to complete-reclaiming after sewage disposal, economized on water in running, without outer blowdown
Water, sludge, without adding medicament, non-secondary pollution, treatment water is sterilized by filtering, meets reuse needs, and floor space is small, if
Standby integrated level is high.
Brief description of the drawings
Fig. 1 is overall structure diagram of the present invention；
Fig. 2 is top view of the present invention；
Fig. 3 sets figure for the rear duct of apparatus of the present invention.
In figure：1- foul water tanks, 2- regulating tanks, 3- is anaerobic fluidized bed, 4- interior circulation aerobe reactors, 5- ozone
Tower, 6- activated carbon adsorbers, 7- filtered water tanks, 8- supernatant water tanks, 9- ozone generators, 10- reamer high-performance water pumps, 11- pipelines
Pump, 12- circulating pumps, 13- perforation water distributors, 14- biologic packing materials, 15- inner cylinders, 16- aeration heads, 17- biologic packing materials, 18- micropores
Aeration head, 19- screen clothes, 20- gravel layers, 21- quartz sand layers, 22- seed activity layer of charcoal, 23- backwash pumps, 24- air pumps,
25- ozone tail gas digestion instruments.
Specific embodiment
The present invention is further illustrated below in conjunction with the accompanying drawings, but the present invention must not be any limitation as by any way,
Based on present invention teach that any change or improvement made, belong to protection scope of the present invention.
As shown in accompanying drawing 1 ~ 3, the present invention includes foul water tank 1, regulating tank 2, anaerobic fluidized bed 3, interior circulation aerobe
Reactor 4, ozone tower 5, activated carbon adsorber 6, lower filtered water tank 7 and supernatant water tank 8, the described connection closet of foul water tank 1 are described
Foul water tank 1 be connected to the top of regulating tank 2, the bottom of regulating tank 2 connects anaerobic fluidized bed 3 bottom, detests by pipeline pump 11
The top of oxygen fluid bed 3 connects the bottom of interior circulation aerobe reactor 4, the top of interior circulation aerobe reactor 4 connection ozone
The bottom of tower 5, the top of ozone tower 5 connection activated carbon adsorber 6 top, the lower filtered water tank 7 of the bottom of activated carbon adsorber 6 connection is lower clear
Water tank 7 connects supernatant water tank 8 by backwash pump 23, and supernatant water tank 8 connects the waste preventer of closet；Described charcoal absorption
The top of tower 6 connects regulating tank 2；The described bottom of interior circulation aerobe reactor 4 connection regulating tank 2；Followed in described
The inside of ring aerobe reactor 4 sets inner cylinder 15, and the bottom of inner cylinder 15 tightly sets aeration head 16, and aeration head 16 passes through pipeline and air
Pump 24 is connected, and the outer top of inner cylinder 15 sets biologic packing material 17；Described ozone tower 5 sets micropore with the bottom of activated carbon adsorber 6
Aeration head 18 connects ozone generator 9, and described ozone tower 5 is connected ozone tail gas with the top of activated carbon adsorber 6 by pipeline
Digestion instrument 25.The described preferred microporous of micro porous aeration head 18 aeration titanium plate, micro porous aeration head 18 is by ozone dissipation into small
Bubble, increases the contacting efficiency of ozone and water, it is possible to decrease colourity, the water pollutant after leading portion is processed further is degraded, and is disappeared
Poisoning bacterium, reduces water outlet bacterial content.The present apparatus is set gradually filth disposal up and down by water inlet, water outlet between each processor
During dirt collection, anaerobism, aerobic, sterilization, filtering combine in a flow, dirt is collected to be formed by regulating tank 2 and is kept in short-term,
Shunt volume enters the interior circulation aerobe reactor that bilayer is provided with interior barrel structure after carrying out just treatment into anaerobic fluidized bed 3
In 4, and the bottom of inner cylinder 15 tightly sets aeration head 16, and aeration head 16 forms certain sinking with the bottom of interior circulation aerobe reactor 4
Shallow lake area, current form interior circulation under the promotion of aeration head 16, and be arranged at top biologic packing material 17 outside inner cylinder then can be sufficient
Biological treatment is carried out, the dirt that cannot be processed completely after treatment sends back to regulating tank 2 and decomposed again again, and in order to ensure
Water quality it is up to standard, carried out ozonization, filtering layer filtering two-layer treatment.
In described anaerobic fluidized bed 3, bottom is provided with perforation water distributor 13, and perforation water distributor 13 is connected with circulating pump 12,
Circulating pump 12 is connected by pipeline with anaerobic fluidized bed 3 top, and anaerobic fluidized bed 3 top sets biologic packing material.Anaerobism stream
Change the water inlet of bed 3 and be located at bottom, water outlet is located at top, and drainage flow direction is that from bottom to top, the installation direction of circulating pump 12 is downward,
Sludge content less water in top is pressurizeed into the perforation water distributor of anaerobic fluidized bed 3 bottom by circulating pump 12, makes fluidisation
Bed bottom activated sludge is in suspended state, can be fully contacted with sewage, improves treatment effeciency.It is filled with anaerobic fluidized bed 3
The carrier that particle diameter is small, specific surface area is big, the biomembrane of anaerobe composition grows in carrier surface, and carrier is in fluidisation shape
State, with good mass transfer condition, microorganism is easily fully contacted with waste water, and bacterium has activity very high, equipment treatment effeciency
It is high.
Screen cloth 19 is set in described activated carbon adsorber 6, gravel layer 20, quartz sand layer is set from the bottom up on screen cloth 19
21st, seed activity layer of charcoal 22, then be configured according to the density of filtering layer, the treatment effect that can be increased water quality.
The water inlet pipe and activated carbon adsorber 6 of the connection supernatant of backwash pump 23 water tank 8 are set in described lower filtered water tank 7
Bottom.The backwash pump 23 changes the effect that water pump and backwash pump are lifted as clear water by motor-driven valve, works as activated carbon
When adsorption tower is backwashed, activated carbon adsorber Inlet and outlet water valve is closed, opens the backwashing pump in filtered water tank, backwashed,
When filtered water tank water reaches low water level, backwashing pump is closed, open activated carbon adsorber Inlet and outlet water valve, backwash terminates；Day
Often work is made single to be used as clear water lifting water pump when not backwashed, and the water of lower filtered water tank 7 is sent into supernatant water tank
8。
Described foul water tank 1, regulating tank 2, anaerobic fluidized bed 3, interior circulation aerobe reactor 4, ozone tower 5, work
The property charcoal adsorption tower 6, connecting pipe between lower filtered water tank 7 and supernatant water tank 8, closet may be contained within a plane, be easy to pipeline
And each device is installed and maintenance.
Described foul water tank 1, regulating tank 2, anaerobic fluidized bed 3, interior circulation aerobe reactor 4, ozone tower 5, work
Property is respectively provided with control valve on the connecting pipe between charcoal adsorption tower 6, lower filtered water tank 7 and the device of supernatant water tank 8.
Described anaerobic fluidized bed 3, interior circulation aerobe reactor 4, ozone tower 5, activated carbon adsorber 6, lower clear water
Case 7 and supernatant water tank 8, bottom is respectively provided with blow-down pipe.
Operation principle of the present invention and the course of work：
The present invention uses " anaerobic fluidized bed+interior circulation aerobe reactor+ozone+activated carbon process " handling process, will sit
（Squat）By elevator pump by sewage collecting to regulating tank, regulating tank sets pipeline pump by sewage lifting to anaerobism to toilet drainage
Fluid bed, water outlet enters interior circulation aerobe reactor, and subsequently into ozone tower, ozone tower water outlet enters charcoal absorption
Tower, final outflow water drains into filtered water tank storage, is promoted to supernatant water tank for sitting（Squat）Closet is used, ozone tower and activated carbon adsorber
Ozone is added, residual ozone sets ozone digestion instrument, arranged outward after residual ozone is decomposed into oxygen.Floor space of the present invention
Small, treatment effeciency is high, device integration is high, need not add medicament, non-secondary pollution, reach zero-emission.
During work, sewage lifting to regulating tank 2 is stored；Regulating tank 2 is repeatedly carried by the pressurization component of pipeline pump 11
Rise and enter in sewage fluid bed 3；Anaerobic fluidized bed 3 staving outside sets circulating pipe pump 12, and top sludge content is less
Sewage is pressurizeed by circulating pump 12 and enters the perforation water distributor 13 of fluidized-bed bottom, is in the bottom activated sludge of fluid bed 3 outstanding
Floating state, can be fully contacted with sewage；It is anti-that water after anaerobic fluidized bed 3 treatment enters interior circulation aerobe from fluid bed top
Answer device 4；Aeration and oxygenation for sewage and contacted with filler in interior circulation aerobe reactor 4, the water after treatment enters ozone tower, instead
Answer device bottom mud to be lifted by stripping regime to return in regulating tank；The bottom of ozone tower 5 sets micro porous aeration head, ozone and sewage
It is fully contacted, water outlet enters activated carbon adsorber 6 from the top of ozone tower 5；The bottom of activated carbon adsorber 6 adds ozone, sewage warp
Activated carbon is filtered and finished with ozone contact post processing, is stored into filtered water tank 7；Clarified water pump 23 is set in clear water reserviors 7, will be located
Water after reason passes through the supreme filtered water tank of Pipeline lift；The water outlet of supernatant water tank 8 gravity flow delivers to each sanitary apparatus to water spot；Filtered water tank 7
Middle setting backwashing pump 23, when activated carbon adsorber 6 is backwashed, closes the Inlet and outlet water valve of activated carbon adsorber 6, opens clear water
Backwashing pump 23 in case 7, is backwashed, and when the water of filtered water tank 7 reaches low water level, closes backwashing pump 23, opens activity
The Inlet and outlet water valve of charcoal adsorption tower 6, backwash terminates；Backwash is drained into regulating tank 2, reuse after being processed again.
Claims (7)
1. a kind of ecological environment protection toilet processing unit, including foul water tank（1）, regulating tank（2）, it is anaerobic fluidized bed（3）, interior circulation
Aerobe reactor（4）, ozone tower（5）, activated carbon adsorber（6）, lower filtered water tank（7）With supernatant water tank（8）, described dirt
Water tank（1）Connection closet, it is characterised in that described foul water tank（1）It is connected to regulating tank（2）Top, regulating tank（2）Under
Portion passes through pipeline pump（11）Connection is anaerobic fluidized bed（3）Bottom, it is anaerobic fluidized bed（3）Top connects interior circulation aerobe reaction
Device（4）Bottom, interior circulation aerobe reactor（4）Top connects ozone tower（5）Bottom, ozone tower（5）Top connection activity
Charcoal adsorption tower（6）Top, activated carbon adsorber（6）The lower filtered water tank of bottom connection（7）, lower filtered water tank（7）By backwash pump
（23）Connection supernatant water tank（8）, supernatant water tank（8）Connect the waste preventer of closet；Described activated carbon adsorber（6）Top connects
Regulating tank（2）；Described interior circulation aerobe reactor（4）Bottom connects regulating tank（2）；Described interior circulation is aerobic
Bioreactor（4）Inside sets inner cylinder（15）, inner cylinder（15）Bottom tightly sets aeration head（16）, aeration head（16）By pipeline with
Air pump（24）Connection, the outer top of inner cylinder sets biologic packing material（17）；Described ozone tower（5）With activated carbon adsorber（6）Bottom
Portion sets micro porous aeration head（18）Connection ozone generator（9）, described ozone tower（5）With activated carbon adsorber（6）Top leads to
Piping connects ozone tail gas digestion instrument（25）.
2. ecological environment protection toilet processing unit according to claim 1, it is characterised in that described is anaerobic fluidized bed（3）
Interior, bottom is provided with perforation water distributor（13）, water distributor of perforating（13）With circulating pump（12）Connection, circulating pump（12）By pipeline with
It is anaerobic fluidized bed（3）Top connects, described anaerobic fluidized bed（3）Top sets biologic packing material.
3. ecological environment protection toilet processing unit according to claim 1, it is characterised in that described activated carbon adsorber（6）
Interior setting screen cloth（19）, screen cloth（19）On gravel layer is set from the bottom up（20）, quartz sand layer（21）, seed activity layer of charcoal
（22）.
4. ecological environment protection toilet processing unit according to claim 1, it is characterised in that described lower filtered water tank（7）Inside set
Put backwash pump（23）Connection supernatant water tank（8）Water inlet pipe and activated carbon adsorber（6）Bottom.
5. ecological environment protection toilet processing unit according to claim 1, it is characterised in that described foul water tank（1）, regulation
Water tank（2）, it is anaerobic fluidized bed（3）, interior circulation aerobe reactor（4）, ozone tower（5）, activated carbon adsorber（6）, it is lower clear
Water tank（7）With supernatant water tank（8）, the connecting pipe between closet may be contained within a plane.
6. ecological environment protection toilet processing unit according to claim 1, it is characterised in that described foul water tank（1）, regulation
Water tank（2）, it is anaerobic fluidized bed（3）, interior circulation aerobe reactor（4）, ozone tower（5）, activated carbon adsorber（6）, it is lower clear
Water tank（7）With supernatant water tank（8）Control valve is respectively provided with connecting pipe between device.
7. ecological environment protection toilet processing unit according to claim 1, it is characterised in that described is anaerobic fluidized bed（3）、
Interior circulation aerobe reactor（4）, ozone tower（5）, activated carbon adsorber（6）With supernatant water tank（8）Bottom is respectively provided with emptying
Pipe.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201710238214.6A CN106927636A (en) | 2017-04-13 | 2017-04-13 | A kind of ecological environment protection toilet processing unit |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201710238214.6A CN106927636A (en) | 2017-04-13 | 2017-04-13 | A kind of ecological environment protection toilet processing unit |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN106927636A true CN106927636A (en) | 2017-07-07 |
Family
ID=59438332
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201710238214.6A Pending CN106927636A (en) | 2017-04-13 | 2017-04-13 | A kind of ecological environment protection toilet processing unit |
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Cited By (4)
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| CN108824580A (en) * | 2018-08-03 | 2018-11-16 | 安徽正风环保设备有限公司 | The ecological environment protection mobile toilet and processing method of circulating water flushing |
| CN110512902A (en) * | 2018-05-21 | 2019-11-29 | 上海华业环保有限公司 | A kind of environmentally friendly bathroom of A2NJBR jet-loop biomembrane process |
| CN110902960A (en) * | 2019-12-09 | 2020-03-24 | 河北华沃环保科技有限责任公司 | Microbial circulating water treatment system for toilet |
| CN111039524A (en) * | 2020-01-09 | 2020-04-21 | 王晓敏 | Integration fecal sewage treatment equipment |
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| CN110512902A (en) * | 2018-05-21 | 2019-11-29 | 上海华业环保有限公司 | A kind of environmentally friendly bathroom of A2NJBR jet-loop biomembrane process |
| CN108824580A (en) * | 2018-08-03 | 2018-11-16 | 安徽正风环保设备有限公司 | The ecological environment protection mobile toilet and processing method of circulating water flushing |
| CN110902960A (en) * | 2019-12-09 | 2020-03-24 | 河北华沃环保科技有限责任公司 | Microbial circulating water treatment system for toilet |
| CN111039524A (en) * | 2020-01-09 | 2020-04-21 | 王晓敏 | Integration fecal sewage treatment equipment |
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