CN206666341U - 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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- CN206666341U CN206666341U CN201720382648.9U CN201720382648U CN206666341U CN 206666341 U CN206666341 U CN 206666341U CN 201720382648 U CN201720382648 U CN 201720382648U CN 206666341 U CN206666341 U CN 206666341U
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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 25
- 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 81
- 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
- 239000000463 material Substances 0.000 claims description 10
- 239000003610 charcoal Substances 0.000 claims description 9
- 230000000694 effects Effects 0.000 claims description 9
- 238000001179 sorption measurement Methods 0.000 claims description 9
- 230000029087 digestion Effects 0.000 claims description 6
- 239000004744 fabric Substances 0.000 claims description 4
- 239000006004 Quartz sand Substances 0.000 claims description 3
- 238000006243 chemical reaction Methods 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 8
- 239000010802 sludge Substances 0.000 abstract description 8
- 238000001914 filtration Methods 0.000 abstract description 6
- 230000008569 process Effects 0.000 abstract description 6
- 238000004659 sterilization and disinfection Methods 0.000 abstract description 6
- 239000002351 wastewater Substances 0.000 abstract description 5
- 239000003814 drug Substances 0.000 abstract description 3
- 230000010354 integration Effects 0.000 abstract description 3
- 229910052799 carbon Inorganic materials 0.000 abstract description 2
- 238000011010 flushing procedure Methods 0.000 abstract description 2
- 230000009965 odorless effect Effects 0.000 abstract description 2
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 6
- 239000001301 oxygen Substances 0.000 description 6
- 229910052760 oxygen Inorganic materials 0.000 description 6
- 238000011001 backwashing Methods 0.000 description 5
- 239000007789 gas Substances 0.000 description 5
- 241000894006 Bacteria Species 0.000 description 4
- 244000005700 microbiome Species 0.000 description 4
- 239000012530 fluid Substances 0.000 description 3
- 238000005243 fluidization Methods 0.000 description 3
- 206010059410 Faecaluria Diseases 0.000 description 2
- 229910002651 NO3 Inorganic materials 0.000 description 2
- NHNBFGGVMKEFGY-UHFFFAOYSA-N Nitrate Chemical compound [O-][N+]([O-])=O NHNBFGGVMKEFGY-UHFFFAOYSA-N 0.000 description 2
- 230000008859 change Effects 0.000 description 2
- 210000003608 fece Anatomy 0.000 description 2
- 238000007667 floating Methods 0.000 description 2
- 238000009434 installation Methods 0.000 description 2
- 238000012423 maintenance Methods 0.000 description 2
- 238000004064 recycling Methods 0.000 description 2
- 239000007790 solid phase Substances 0.000 description 2
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 1
- RTAQQCXQSZGOHL-UHFFFAOYSA-N Titanium Chemical compound [Ti] RTAQQCXQSZGOHL-UHFFFAOYSA-N 0.000 description 1
- 238000010521 absorption reaction Methods 0.000 description 1
- XKMRRTOUMJRJIA-UHFFFAOYSA-N ammonia nh3 Chemical compound N.N XKMRRTOUMJRJIA-UHFFFAOYSA-N 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
- -1 disinfection Substances 0.000 description 1
- 230000005611 electricity Effects 0.000 description 1
- 238000004134 energy conservation Methods 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 230000007613 environmental effect Effects 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
- 239000007788 liquid Substances 0.000 description 1
- 230000002906 microbiologic effect Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification 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
- 238000006213 oxygenation 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
- 231100000719 pollutant Toxicity 0.000 description 1
- 238000012805 post-processing Methods 0.000 description 1
- 238000011002 quantification Methods 0.000 description 1
- 230000009467 reduction Effects 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
- 230000001954 sterilising effect Effects 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
- 238000012549 training Methods 0.000 description 1
- 238000012546 transfer Methods 0.000 description 1
- 230000032258 transport Effects 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
Landscapes
- Treatment Of Water By Oxidation Or Reduction (AREA)
- Water Treatment By Sorption (AREA)
Abstract
The utility model 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,Pass through 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 connected up and down successively,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,Pass through anaerobism,It is aerobic,Disinfection,Water body is filtered,The reclaimed water up to standard for forming colorless and odorless returns again to use of flushing the toilet,Economized on water in running,Without externally discharged waste water,Sludge,Medicament need not be added,Non-secondary pollution,Water is handled to sterilize by filtering,Meet reuse needs,Floor space is small,Device integration is high.
Description
Technical field
The utility model belongs to wastewater reusing device technical field, and in particular to a kind of environment-friendly water-saving, water body is recyclable to be made
Ecological environment protection toilet processing unit.
Background technology
Bio-toilet is intended to economize on water, saved, and by mankind's fecaluria, recycling, innoxious and minimizing are handled on the spot, main to use
In open air without perfect water and electricity supply and the place of 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 uses are that excreta entrance is arranged on lavatory collective low system, utilize stirring system
System is sufficiently stirred to slop and with agricultural crop straw or wood chip etc. for the biological dispensing of main component, and is added
Heat, moisture evaporation is acted on by the biochemical degradation of microorganism aerobic bacterium, by mankind's fecaluria recycling, innoxious and subtract on the spot
Quantification treatment, the bio-feritlizer that final output is dried.There is water type bio-toilet often using with environmental project method, blowdown
After separation of solid and liquid, reuse after processing harmless treatment is carried out to liguid phase pollutant, solid phase transports outward after-treatment by packing.It is anhydrous
Type bio-toilet not water consumption, energy-conservation, but the problem of smell and bad clean environment be present.There is water type bio-toilet once to add water,
As supplement recycle-water after by the use of urine process, water saving, processing power consumption is higher than anhydrous type bio-toilet, solid waste be present and beats
Reason trouble is assured, the problem of maintenance is difficult, and clean environment is bad, while backwater seldom carries out disinfection processing, causes 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
More bio-toilets can not be effectively treated in time.Therefore, emergency case can be tackled by developing one kind, only need to once add
Water, water saving in running, without draining, excreta realize 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 that can be recycled to waste water up to standard
Solves the effective way of this problem.
Utility model content
The purpose of this utility model be to provide it is a kind of it is compact-sized, be easy to implement, energy consumption is low, efficiently, the ecology of water saving
Environment protection water closet processing unit.
The purpose of this utility model is achieved in that including foul water tank, regulating tank, anaerobic fluidized bed, interior circulated
Oxygen bioreactor, ozone tower, activated carbon adsorber, lower filtered water tank and supernatant water tank, described foul water tank connection closet are described
Foul water tank be connected to regulating tank top, regulating tank bottom connects anaerobic fluidized bed bottom, anaerobism fluidisation by pipeline pump
Circulation aerobe reactor bottom in the connection of bed top, interior circulation aerobe reactor top connection ozone tower bottom are smelly
Oxygen column top connection activated carbon adsorber top, the lower filtered water tank of activated carbon adsorber bottom connection, lower filtered water tank pass through backwash
Water pump connects supernatant water tank, and supernatant water tank connects the waste preventer of closet；Described activated carbon adsorber top connection regulating tank；
Described interior circulation aerobe reactor bottom connection regulating tank；Set inside described interior circulation aerobe reactor
Inner cylinder, inner cylinder bottom tightly set aeration head, and aeration head is connected by pipeline with air pump, and the outer top of inner cylinder sets biologic packing material；Institute
The ozone tower stated sets micro porous aeration head to be connected ozone generator, described ozone tower and activated carbon with charcoal absorption tower bottom
Ozone tail gas digestion instrument is connected by pipeline at the top of adsorption tower.
The utility model by foul water tank, regulating tank, it is anaerobic fluidized bed, it is interior circulation aerobe reactor, ozone tower,
Activated carbon adsorber, lower filtered water tank, the upper and lower successively of supernatant water tank are connected, by anaerobic fluidized bed, interior circulation aerobe reaction
The sewage treatment process such as device, ozone, active carbon purifying are integrated in one, and high-concentration sewage is collected, by anaerobism, good
Oxygen, disinfection, water body are filtered, and the reclaimed water up to standard for forming colorless and odorless returns again to use of flushing the toilet；And activated carbon adsorber
Top and interior circulation aerobe reactor bottom all connect regulating tank, can will be unable to the flow that the part dirt of processing is sent back to
Starting point carries out circular treatment again, improves processing quality；Interior circulation aerobe reactor sets inner cylinder, and inner cylinder bottom tightly sets exposure
Gas head, aeration head are connected by pipeline with air air pump, bucket internal upper part setting biologic packing material, in inner cylinder aeration process, on bubble
It is floating, drive the sewage of bottom to run up, in inner cylindrical into aerobic zone, the water (flow) direction of outer barrel from top to bottom, it is barrel-shaped outside into
Anoxic zone, inner/outer tube current form circulation, the biologic packing material that bucket internal upper part is set, and sewage is oxygenated repeatedly, bubble and microorganism
Cenobium is refined by continuous shearing, and forms fine and close tiny floccule body, and in aerobic zone, organic pollution is decomposed by microbiological oxidation,
The ammonia nitrogen in sewage is converted into nitrate by the nitrification of microorganism simultaneously, and anti-nitration reaction, anti-nitre are carried out in anoxic zone
To change bacterium under anoxic conditions, reduce nitrate, discharge molecular nitrogen (N2), activated sludge gradually sinks to reactor bottom, on
Layer water becomes clear, is carried out disinfection into ozone tower, is filtered afterwards into activated carbon adsorber；Biological treatment needs the regular hour,
And the setting of regulating tank then can play a part of buffer when flow of the people increases suddenly；Ozone tail gas digestion instrument is set
Put, residual ozone can be decomposed into after oxygen it is outer arrange, nearby oxygen is sufficient for device in running, reduces stink and unplessantness displeasure.
The utility model is compact-sized, and whole handling process is combined in a device, to complete-reclaiming after sewage disposal, in running
Water saving, no externally discharged waste water, sludge, without adding medicament, non-secondary pollution, processing water sterilizes by filtering, meets reuse needs,
Floor space is small, and device integration is high.
Brief description of the drawings
Fig. 1 is the utility model overall structure diagram；
Fig. 2 is the utility model top view；
Fig. 3 is that the rear duct of the utility model device sets figure.
In figure：1- foul water tanks, 2- regulating tanks, 3- is anaerobic fluidized bed, circulation aerobe reactor, 5- ozone in 4-
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.
Embodiment
The utility model is further described below in conjunction with the accompanying drawings, but the utility model must not be added in any way
With limitation, any changes and modifications made based on the utility model training centre, the scope of protection of the utility model is belonged to.
As shown in accompanying drawing 1 ~ 3, it is aerobic that the utility model includes foul water tank 1, regulating tank 2, anaerobic fluidized bed 3, interior circulation
Bioreactor 4, ozone tower 5, activated carbon adsorber 6, lower filtered water tank 7 and supernatant water tank 8, described foul water tank 1 connection closet,
Described foul water tank 1 is connected to the top of regulating tank 2, and the bottom of regulating tank 2 is connected under anaerobic fluidized bed 3 by pipeline pump 11
Portion, anaerobic fluidized bed interior circulation aerobe reactor 4 bottom of 3 top connection, the connection of interior circulation aerobe reactor 4 top
The bottom of ozone 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,
Lower filtered water tank 7 connects supernatant water tank 8 by backwash pump 23, and supernatant water tank 8 connects the waste preventer of closet；Described activated carbon
The top of adsorption tower 6 connects regulating tank 2；The described interior bottom of circulation aerobe reactor 4 connection regulating tank 2；Described
Interior circulation aerobe reactor 4 inside sets inner cylinder 15, and the bottom of inner cylinder 15 tightly sets aeration head 16, aeration head 16 by pipeline with
Air pump 24 connects, and 15 outer top of inner cylinder sets biologic packing material 17；Described ozone tower 5 is set with the bottom of activated carbon adsorber 6
Micro porous aeration head 18 connects ozone generator 9, and described ozone tower 5 is connected ozone with the top of activated carbon adsorber 6 by pipeline
Tail gas 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 Cheng Wei
Small bubble, increase the contacting efficiency of ozone and water, colourity can be reduced, the water pollutant after leading portion is handled further drops
Solution, disinfection, reduce water outlet bacterial content.The present apparatus between each processor by being intake, water outlet is set gradually dirt up and down
The dirt collection of processing, anaerobism, aerobic, sterilization, filtering are combined in a flow, dirt is collected by regulating tank 2 to be formed it is short
When keep in, shunt volume, which enters anaerobic fluidized bed 3, to carry out entering bilayer after just handling and is provided with the aerobic lifes of interior circulation of interior barrel structure
In thing reactor 4, and the bottom of inner cylinder 15 tightly sets aeration head 16, and aeration head 16 is formed with interior circulation aerobe reactor 4 bottom
Certain settling zone, current formed under the promotion of aeration head 16 in circulation, and be arranged at outside inner cylinder top biologic packing material 17 then
Biological treatment can be sufficiently carried out, the dirt that can not be handled completely after processing sends back to regulating tank 2 and decomposed again again, and
In order to ensure the up to standard of water quality, ozonization, two layers of processing of filtering layer filtering have been carried out.
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
To 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 fully be 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 grow in carrier surface, and carrier is in fluidisation shape
State, there is good mass transfer condition, microorganism easily fully contacts with waste water, and bacterium has very high activity, equipment treatment effeciency
It is high.
Screen cloth 19 is set in described activated carbon adsorber 6, gravel layer 20, quartz sand layer are set from the bottom up on screen cloth 19
21st, seed activity layer of charcoal 22, then it is configured according to the density of filtering layer, the treatment effect that can be increased water quality.
Backwash pump 23 is set to connect the water inlet pipe and activated carbon adsorber 6 of supernatant water tank 8 in described lower filtered water tank 7
Bottom.The backwash pump 23 lifts the effect of water pump and backwash pump by motor-driven valve conversion as clear water, works as activated carbon
When adsorption tower backwashes, activated carbon adsorber Inlet and outlet water valve is closed, the backwashing pump in filtered water tank is opened, is backwashed,
When filtered water tank water reaches low water level, backwashing pump is closed, opens activated carbon adsorber Inlet and outlet water valve, backwash terminates；Day
Often work single can be used as clear water lifting water pump to use without making during backwash, and the water of lower filtered water tank 7 is sent into supernatant water tank
8。
It is described foul water tank 1, regulating tank 2, anaerobic fluidized bed 3, interior circulation aerobe reactor 4, ozone tower 5, living
Connecting pipe between property charcoal adsorption tower 6, lower filtered water tank 7 and supernatant water tank 8, closet may be contained within a plane, be easy to pipeline
And each device installation and maintenance.
It is described foul water tank 1, regulating tank 2, anaerobic fluidized bed 3, interior circulation aerobe reactor 4, ozone tower 5, living
Control valve is respectively provided with connecting pipe between property 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.
Utility model works principle and the course of work：
The utility model is using " anaerobic fluidized bed+interior circulation aerobe reactor+ozone+activated carbon process " processing stream
Journey, it will sit（Squat）Sewage collecting to regulating tank, regulating tank are set pipeline pump to carry sewage by toilet drainage by elevator pump
Rise to anaerobic fluidized bed, water outlet enters interior circulation aerobe reactor, and subsequently into ozone tower, the water outlet of ozone tower enters activity
Charcoal adsorption tower, final outflow water drain into filtered water tank storage, are promoted to supernatant water tank for sitting（Squat）Closet uses, ozone tower and activated carbon
Adsorption tower adds ozone, and residual ozone sets ozone digestion instrument, and residual ozone is decomposed into after oxygen and arranged outside.The utility model
Floor space is 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；Circulating pipe pump 12 is set outside anaerobic fluidized bed 3 staving, top sludge content is less
Perforation water distributor 13 of the sewage by the pressurization of circulating pump 12 into fluidized-bed bottom, makes the bottom activated sludge of fluid bed 3 be in outstanding
Floating state, can fully be contacted with sewage；Water after anaerobic fluidized bed 3 processing is anti-from fluid bed top into interior circulation aerobe
Answer device 4；Interior to circulate aeration and oxygenation for sewage in aerobe reactor 4 and contacted with filler, the water after processing enters ozone tower, instead
Device bottom mud is answered to be returned to by stripping regime lifting in regulating tank；The bottom of ozone tower 5 sets micro porous aeration head, ozone and sewage
Fully contact, water outlet enter 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 backwashes, 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, is closed backwashing pump 23, is opened activity
The Inlet and outlet water valve of charcoal adsorption tower 6, backwash terminate；Backwash is drained into regulating tank 2, reuse after being handled 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）Connect 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）Connect anaerobic fluidized bed（3）Bottom, it is anaerobic fluidized bed（3）Circulation aerobe reaction in the connection of top
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）Pass through backwash pump
（23）Connect 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 set biologic packing material（17）；Described ozone tower（5）With activated carbon adsorber（6）Bottom
Portion sets micro porous aeration head（18）Connect 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）Connect 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 |
|---|---|---|---|
| CN201720382648.9U CN206666341U (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 |
|---|---|---|---|
| CN201720382648.9U CN206666341U (en) | 2017-04-13 | 2017-04-13 | A kind of ecological environment protection toilet processing unit |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206666341U true CN206666341U (en) | 2017-11-24 |
Family
ID=60381474
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201720382648.9U Expired - Fee Related CN206666341U (en) | 2017-04-13 | 2017-04-13 | A kind of ecological environment protection toilet processing unit |
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Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106927636A (en) * | 2017-04-13 | 2017-07-07 | 昆明重工佳盛慧洁特种设备制造有限公司 | A kind of ecological environment protection toilet processing unit |
| CN109809645A (en) * | 2019-03-21 | 2019-05-28 | 四川泰合泰环境工程有限公司 | A kind of the night soil treatment system and its technique of not power consumption |
| CN110902974A (en) * | 2019-12-19 | 2020-03-24 | 北京清核朝华科技有限公司 | Sewage deep purification and water quality improvement treatment system and method |
-
2017
- 2017-04-13 CN CN201720382648.9U patent/CN206666341U/en not_active Expired - Fee Related
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106927636A (en) * | 2017-04-13 | 2017-07-07 | 昆明重工佳盛慧洁特种设备制造有限公司 | A kind of ecological environment protection toilet processing unit |
| CN109809645A (en) * | 2019-03-21 | 2019-05-28 | 四川泰合泰环境工程有限公司 | A kind of the night soil treatment system and its technique of not power consumption |
| CN110902974A (en) * | 2019-12-19 | 2020-03-24 | 北京清核朝华科技有限公司 | Sewage deep purification and water quality improvement treatment system and method |
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