CN107265820A - A kind of Modularized sewage separation drying process system of intelligent environment protection toilet - Google Patents
A kind of Modularized sewage separation drying process system of intelligent environment protection toilet Download PDFInfo
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- CN107265820A CN107265820A CN201710589794.3A CN201710589794A CN107265820A CN 107265820 A CN107265820 A CN 107265820A CN 201710589794 A CN201710589794 A CN 201710589794A CN 107265820 A CN107265820 A CN 107265820A
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- collecting box
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- 239000010865 sewage Substances 0.000 title claims abstract description 73
- 238000000926 separation method Methods 0.000 title claims abstract description 34
- 238000001035 drying Methods 0.000 title claims abstract description 19
- 239000007788 liquid Substances 0.000 claims abstract description 48
- 239000000843 powder Substances 0.000 claims abstract description 45
- 239000011941 photocatalyst Substances 0.000 claims abstract description 17
- 238000005119 centrifugation Methods 0.000 claims abstract description 16
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 30
- 238000010079 rubber tapping Methods 0.000 claims description 20
- 239000007921 spray Substances 0.000 claims description 17
- 239000002699 waste material Substances 0.000 claims description 14
- 230000008676 import Effects 0.000 claims description 10
- 238000007599 discharging Methods 0.000 claims description 6
- 238000011010 flushing procedure Methods 0.000 claims description 6
- JEGUKCSWCFPDGT-UHFFFAOYSA-N h2o hydrate Chemical compound O.O JEGUKCSWCFPDGT-UHFFFAOYSA-N 0.000 claims description 6
- 238000012856 packing Methods 0.000 claims description 6
- 238000007790 scraping Methods 0.000 claims description 4
- 239000007787 solid Substances 0.000 abstract description 32
- 230000002550 fecal effect Effects 0.000 abstract description 31
- 230000001954 sterilising effect Effects 0.000 abstract description 9
- 238000004659 sterilization and disinfection Methods 0.000 abstract description 8
- 238000012423 maintenance Methods 0.000 abstract description 5
- 239000004744 fabric Substances 0.000 description 13
- 239000012528 membrane Substances 0.000 description 13
- 238000012545 processing Methods 0.000 description 12
- 238000001514 detection method Methods 0.000 description 6
- 239000002893 slag Substances 0.000 description 6
- 238000005516 engineering process Methods 0.000 description 4
- 239000000463 material Substances 0.000 description 4
- 238000000034 method Methods 0.000 description 4
- 238000004140 cleaning Methods 0.000 description 3
- 239000012535 impurity Substances 0.000 description 3
- 238000001816 cooling Methods 0.000 description 2
- 230000018044 dehydration Effects 0.000 description 2
- 238000006297 dehydration reaction Methods 0.000 description 2
- 239000003651 drinking water Substances 0.000 description 2
- 235000020188 drinking water Nutrition 0.000 description 2
- 239000003344 environmental pollutant Substances 0.000 description 2
- 210000003608 fece Anatomy 0.000 description 2
- 231100000719 pollutant Toxicity 0.000 description 2
- 230000008439 repair process Effects 0.000 description 2
- ATJFFYVFTNAWJD-UHFFFAOYSA-N Tin Chemical compound [Sn] ATJFFYVFTNAWJD-UHFFFAOYSA-N 0.000 description 1
- 230000005540 biological transmission Effects 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 239000003818 cinder Substances 0.000 description 1
- 238000011109 contamination Methods 0.000 description 1
- 230000000593 degrading effect Effects 0.000 description 1
- 230000001877 deodorizing effect Effects 0.000 description 1
- 239000000645 desinfectant Substances 0.000 description 1
- 230000000249 desinfective effect Effects 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000011049 filling Methods 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 238000003780 insertion Methods 0.000 description 1
- 230000037431 insertion Effects 0.000 description 1
- 230000007246 mechanism Effects 0.000 description 1
- 244000005700 microbiome Species 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 239000003895 organic fertilizer Substances 0.000 description 1
- 230000000149 penetrating effect Effects 0.000 description 1
- 230000008569 process Effects 0.000 description 1
- 238000010298 pulverizing process Methods 0.000 description 1
- 239000010802 sludge Substances 0.000 description 1
- 239000002689 soil Substances 0.000 description 1
- 238000004065 wastewater treatment Methods 0.000 description 1
- 238000004804 winding Methods 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
- C02F11/00—Treatment of sludge; Devices therefor
- C02F11/12—Treatment of sludge; Devices therefor by de-watering, drying or thickening
- C02F11/121—Treatment of sludge; Devices therefor by de-watering, drying or thickening by mechanical de-watering
- C02F11/127—Treatment of sludge; Devices therefor by de-watering, drying or thickening by mechanical de-watering by centrifugation
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/34—Chemical or biological purification of waste gases
- B01D53/74—General processes for purification of waste gases; Apparatus or devices specially adapted therefor
- B01D53/86—Catalytic processes
-
- 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
- C02F1/20—Treatment of water, waste water, or sewage by degassing, i.e. liberation of dissolved gases
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F11/00—Treatment of sludge; Devices therefor
- C02F11/12—Treatment of sludge; Devices therefor by de-watering, drying or thickening
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F11/00—Treatment of sludge; Devices therefor
- C02F11/18—Treatment of sludge; Devices therefor by thermal conditioning
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2257/00—Components to be removed
- B01D2257/91—Bacteria; Microorganisms
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2258/00—Sources of waste gases
- B01D2258/02—Other waste gases
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2259/00—Type of treatment
- B01D2259/80—Employing electric, magnetic, electromagnetic or wave energy, or particle radiation
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2303/00—Specific treatment goals
- C02F2303/02—Odour removal or prevention of malodour
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2303/00—Specific treatment goals
- C02F2303/04—Disinfection
Landscapes
- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Environmental & Geological Engineering (AREA)
- Organic Chemistry (AREA)
- Life Sciences & Earth Sciences (AREA)
- Water Supply & Treatment (AREA)
- Hydrology & Water Resources (AREA)
- Mechanical Engineering (AREA)
- Health & Medical Sciences (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Biomedical Technology (AREA)
- Analytical Chemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Treatment Of Sludge (AREA)
- Heat Treatment Of Water, Waste Water Or Sewage (AREA)
Abstract
The Modularized sewage separation drying process system of intelligent environment protection toilet disclosed by the invention, including：Module framework, collecting box, dry powder collecting box, centrifuge drier, heat exchanger, steam trap, jet mixer, photocatalyst device and heater, collecting box, dry powder collecting box, centrifuge drier, heat exchanger, steam trap, jet mixer, photocatalyst device and heater are integrated in module framework, heater produces in high-temperature gas feeding centrifugation drier and on the one hand carries out high temperature sterilization to the fecal sewage centrifuged in drier, on the other hand dried again to centrifuging the solid in drier, form dry powder discharge.The Modularized sewage separation drying process system of the intelligent environment protection toilet of the present invention is easy to integral demounting to get off maintenances, and treating capacity is big, and in separation of solid and liquid, to dirt progress high temperature sterilization so that sewage being capable of reuse.
Description
Technical field
The present invention relates to stool detection technical field, the more particularly to Modularized sewage of intelligent environment protection toilet point
From drying process system.
Background technology
In order to prevent pollution of the fecal sewage to environment, fecal sewage from being located in advance using Physical after typically being concentrated
Reason, i.e., separated the solid content in fecal sewage and water using plant equipment, the solid content isolated can be filled directly, or
It is used as afforestation organic fertilizer after harmless treatment, the sewage separated then is discharged at municipal sewage plant
Reason.
At present, the pretreatment of fecal sewage mainly has following three kinds of modes.
The first processing mode is to carry out separation of solid and liquid to fecal sewage using coarse rack or similar simple device, so
After be discharged into Municipal sewage.This method is simple, but the processing mode can only separate debris a small amount of in fecal sewage
Out, and on the debris separated substantial amounts of excrement can be adhered to, subsequent treatment still has that pollutant concentration is high, and solid content is dense
The problem of degree is also high.
Second of processing mode is first to carry out pulverization process to the solid impurity in fecal sewage, then passes through helical feed
Device carries out separation of solid and liquid.Due to have passed through crushing, the impurity separated moisture content after squeezing can be reduced, organic components
It can also reduce, can directly carry out landfill disposal.But the equipment composition of processing mode needs is complicated, volume is larger, uncomfortable
Close supporting small sewage treatment equipment application.
The third processing mode is to be discharged into sewage treatment plant after carrying out separation of solid and liquid, desanding, dehydration to fecal sewage.At this
Reason mode is not crushed to the impurity in fecal sewage, and the grid equipment of system is easily blocked, and a whole set of processing system
Structure of uniting is increasingly complex, volume bigger, cost is high and operating cost is expensive.
At present, the vehicles such as aircraft, high ferro and motor-car generally collect fecal sewage using vacuum feces collecting technology.This kind of excrement
Just sewage has the characteristics of pollutant concentration is high, solid concentration is high, directly handles such dirt using small sewage treatment equipment
The intractability of water is than larger.Not only wastewater treatment efficiency is undesirable, it is difficult to realize qualified discharge, and it is stifled often to occur sludge
Plug causes equipment downtime.
Application publication number is CN103526825A (Application No. 201310464983.X) Chinese invention patent application《Newly
Type fecal suction truck》, and the Chinese invention patent that application publication number is CN104829013A (Application No. 201510288094.1)
Application《Portable septic tank contamination Intelligent processing system》, wherein disclosed scheme is using dirt of the centrifugal drum to suction
Separation of solid and liquid is carried out, by the processing procedure, solid dirt stays in centrifugal drum, then the subsequent treatment of centrifugal drum is very numb
It is tired, spray equipment is generally also needed to after processing and carries out cleaning showers.The processing procedure of one side solid dirt is complex, another
Aspect is not suitable for using in the intelligent environment protection toilet using vacuum feces collecting technology.
Therefore, a kind of fecal sewage solid-liquid separator disclosed in Chinese invention patent application publication No. CN105174631A,
It includes equipment for separating liquid from solid, feed pipe, deslagging device and the water plug being connected with separation of solid and liquid, and solid for controlling
Liquid separating apparatus, feed pipe, deslagging device and the control device of water plug work.Equipment for separating liquid from solid includes a casing, set
Put in the screen cloth rotary drum that in the casing and can be rotated, screen cloth rotary drum and carry the biologic packing material with microorganism species,
There is the liquid storage area for being used for collecting fecal sewage, the liquid storage area is located at the lower section of screen cloth rotary drum in casing.The fecal sewage solid-liquid
Separator can effectively catching and excrement solid content of degrading, facilitate the subsequent treatment of excrement solid content, fecal sewage solid-liquid point
It is applied to from device on compact apparatus.
A kind of fecal sewage solid-liquid separator disclosed in above-mentioned Chinese invention patent application publication No. CN105174631A, be
Prevent screen pack of the material sticks on screen cloth rotary drum online, be additionally provided with an air jet system, the jet in the casing
Device is located at the top of the screen cloth rotary drum to facilitate the sieve screen apertures on dredging screen cloth rotary drum.
In order to realize that the cleaning of gas in casing is discharged, a venthole, the venthole are offered at the top of the casing
Place is provided with a gas cleaner.One is offered on screen cloth rotary drum, and for maintenance screen cloth rotary drum and into screen cloth rotary drum, filling biology is filled out
Covering is provided with a cover plate on the manhole of material, the manhole.Equipment for separating liquid from solid, which also includes one, to be used to drive the screen cloth
Rotary drum rotate drive device, the drive device include be arranged on outside the casing motor, be connected to the driving
Drive gear on motor driving shaft and the driven gear for being connected to the screen cloth rotary drum side, the motor driving
In shaft extension to casing, the drive gear and the driven gear are located in the casing and energy engaged transmission.For convenience will
Fecal sewage point is sprinkled upon on biologic packing material, the port of export of the feed pipe is extended in the screen cloth rotary drum, and the feed pipe goes out
A flow-stopping plate is provided with above the bend pipe that mouth connection one is bent upwards, the winding pipe exit.The deslagging device includes spiral
Slag tapping equipment and the slag receiving trough being connected with the spiral clinker removor, the main body of the spiral clinker removor are arranged on the casing
Outside, the slag feed pipe of the spiral clinker removor is passed in the screen cloth rotary drum, and the residue outlet of the spiral clinker removor passes to the receipts
In slag chute.The water plug includes suction pump and the drinking-water pipe and outlet pipe that are connected with the suction pump, described to draw water
Pump is arranged on outside the casing, and the drinking-water pipe is passed in the liquid storage area.Liquid level detection device is provided with the liquid storage area,
The liquid level detection device and the suction pump are connected with the control device, and the control device can be according to the liquid
The liquid level data of level detecting apparatus detection controls the start and stop of the suction pump.The liquid level detection device includes at least two liquid levels
Sensor, different liquid level sensor is arranged on the different height and position in the liquid storage area.
A kind of fecal sewage solid-liquid separator disclosed in above-mentioned Chinese invention patent application publication No. CN105174631A point
From inefficiency, be not suitable for the big intelligent environment protection toilet of excrement amount and use, while above-mentioned technology is carrying out solid-liquid to fecal sewage
During separation, not to fecal sewage carry out sterilizing processing, cause sewage can not reuse, while be also not easy to maintenance.
The content of the invention
The technical problems to be solved by the invention are to be directed to used solid-liquid during above-mentioned stool detection
Many technical problems present in separator and to provide a kind of night soil-treatment amount big and excrement can be carried out in separation process
High temperature sterilization is sterilized so that the sewage of separation after treatment can reuse in time, be easy to the intelligent environment protection toilet that repairs
Modularized sewage separates drying process system.
The technical problems to be solved by the invention can be realized by following technical solution：
A kind of Modularized sewage separation drying process system of intelligent environment protection toilet, including：
What one vacuum sewage system being connected with intelligent environment protection toilet was connected is used to collect what intelligent environment protection toilet was discharged
There is the collecting box of excrement, the collecting box dirt outlet, an exhaust outlet, the first dirt circulation interface and the second dirt to follow
Ring interface；
There is one dry powder collecting box, the dry powder collecting box dry powder to collect import and a dry powder discharging opening, the dry powder
The dry powder discharging opening of collecting box is connected with outside dry powder collection device；
One centrifuges drier, be provided with the centrifugation drier dirt entrance, a high-temperature gas entrance,
One dry powder is exported and a waste liquid outlet, and the dirt entrance on the centrifugation drier passes through pipeline, blowdown valve group, sewage pump
It is connected with the dirt outlet on the collecting box；Collected by the dry powder of pipeline and the dry powder collecting box dry powder outlet
Import is connected；
On one heat exchanger, the heat exchanger have first medium entrance, first medium outlet, second medium entrance,
Second medium is exported, and the first medium entrance on the heat exchanger is gone out by the waste liquid of pipeline and the centrifugation drier
Second medium entrance on mouth connection, the heat exchanger is connected with the first dirt circulation interface of the collecting box, the heat
Second medium outlet on exchanger is connected with the second dirt circulation interface of the collecting box；
There is a sewage inlet, a gas vent and an outlet of sewer, institute on one steam trap, the steam trap
The sewage inlet stated on steam trap is connected by pipeline with the first medium outlet on the heat exchanger, the steam point
Water treatment facilities is connected by blowoff valve and pipeline from the outlet of sewer on device；
There is a gas access, gas vent and an air intake on one jet mixer, the jet mixer, it is described
Gas access on jet mixer is connected by pipeline with the gas vent on the steam trap, the jet mixer
On air intake be connected by air shut-off valve group with an air cleaner；On the air cleaner there is an air to enter
Mouthful, the air intake connects an air compressor machine by pipeline；
One photocatalyst device, the photocatalyst device is provided with a gas access and a gas vent, and the light is touched
Gas access on medium/device is connected by pipeline with the gas vent on the jet mixer；
One heater, the heater has on high-temperature gas outlet and a cold wind import, the heater
Cold wind import be connected by pipeline and a blower fan with the gas vent on the photocatalyst device；Height on the heater
Warm gas vent is connected by pipeline with the high-temperature gas entrance on the centrifugation drier；And a module framework, institute
State collecting box, dry powder collecting box, centrifuge drier, heat exchanger, steam trap, jet mixer, photocatalyst device
And heater is integrated in the module framework.
In a preferred embodiment of the invention, the blowdown valve group includes in parallel Stress control blowoff valve and manually
Blowoff valve, wherein Stress control blowoff valve are by the Stress control centrifuged in drier.
In a preferred embodiment of the invention, the air shut-off valve group includes magnetic valve and hand-operated valve in parallel.
In a preferred embodiment of the invention, the centrifugation drier includes：
One shell, the shell is supported by centrifuging machine support, and the centre position of side face one of the shell is provided with one
The high-temperature gas entrance, is provided with a tapping chamber on the right side of the shell, and one is provided with the cavity wall of the tapping chamber
The dry powder outlet；
One axle sets centrifugal network cylinder assembly in the housing, and the centrifugal network cylinder assembly includes net cartridge unit and the net
The left and right rotating shaft that cartridge unit two ends are fixedly connected, the left and right rotating shaft is respectively by left and right bearings in the shell
On left and right side plate, the left and right rotating shaft is hollow rotating shaft；The net cartridge unit be divided into, in, outer net cylinder, it is described it is interior, in,
Outer net cylinder all barrels on be provided with some meshes and it is described it is interior, in, outer net cylinder all barrel inner surfaces on be pasted with life
Thing ventilated membrane, it is described in, in, the barrel chamber of outer net cylinder be sequentially communicated, the barrel chamber of outer net cylinder is connected with the tapping chamber；It is described
Left rotary shaft and centrifugal network cylinder drive device drive connection；
One is located at the auger cylinder in the left rotary shaft in the centrifugal network cylinder assembly by bearing axle, the auger cylinder
Right-hand member is inserted in the barrel chamber of the Intranet cylinder, and the left end of the auger cylinder stretches out the shell, in the auger cylinder left end
Barrel on offer dirt entrance described in one, offer waste liquid outlet described in one on the barrel of the auger cylinder right-hand member,
The dirt entrance is connected by the auger cylinder lumen with the waste liquid outlet；
One is rotatably installed in the feeding auger in the auger cylinder lumen, and the feeding auger includes a screw-conveyer-shaft and one
Spiral way is fixed on inside provided with the axle through the screw-conveyer-shaft in the packing auger blade on the screw-conveyer-shaft, the screw-conveyer-shaft
Hole, radial direction limbers, the radial direction limbers and the axial bore in the screw-conveyer-shaft are offered in the left end of the screw-conveyer-shaft
Connection；
One connector drum, the right-hand member of the connector drum is fixedly connected with the auger cylinder, left end and a reducing gear
Connection, the left end of the screw-conveyer-shaft is slowed down in the connector drum and with described by bearings through the connector drum
The output shaft drive connection of mechanism；Flushing water water inlet pipe, the flushing water water inlet are provided with the barrel of the connector drum
Pipe is connected by the barrel chamber of the connector drum with the radial direction limbers of the screw-conveyer-shaft left end；
One motor being connected with the reducing gear, the input shaft of the output shaft of the motor and the reducing gear drives
Connection；
One spray equipment for being connected and being located in the Intranet cylinder barrel chamber with the screw-conveyer-shaft right-hand member；
One is arranged on the water out adapter in the right spindle in the net cartridge unit, the left end of the water out adapter by bearing
Connected with the barrel chamber of Intranet cylinder, the right-hand member of the water out adapter connects an outlet pipe.
In a preferred embodiment of the invention, the spray equipment includes a shower and installed in the shower
Left, the spray baffle plate by two ends, the inner chamber of the shower is connected with the axial bore in the screw-conveyer-shaft, in the shower
On be arranged at intervals with some spray nozzles.
In a preferred embodiment of the invention, first is provided with the right side of all barrels of Intranet cylinder to slag tap
Hole, the second scum hole is provided with the left of all barrels of the middle net cylinder, and the is provided with the right side end wall of outer net cylinder
Three scum holes；The barrel chamber of the Intranet cylinder is connected by first scum hole with the barrel chamber of the middle net cylinder, the middle net cylinder
Barrel chamber be connected by the barrel chamber of second scum hole and the outer net cylinder, the barrel chamber of the outer net tin goes out by the described 3rd
Cinder hole is connected with the tapping chamber.
In a preferred embodiment of the invention, an observation window is provided with the side face of the shell.
In a preferred embodiment of the invention, a scraper plate, the scraper plate are installed on the right side of the net cartridge unit
In the tapping chamber, circumferentially it is evenly equipped with the scraper plate and some scrapes pawl, the inner surface for scraping pawl and the tapping chamber
Contact.
As a result of technical scheme as above, the Modularized sewage of intelligent environment protection toilet of the invention is separated at dry
Reason system is easy to dismounting to safeguard, treating capacity is big, and in separation of solid and liquid, carries out high temperature sterilization to dirt so that sewage can be returned
With.
Brief description of the drawings
Fig. 1 separates the schematic perspective view of drying process system for the Modularized sewage of the intelligent environment protection toilet of the present invention.
Fig. 2 separates the principle schematic of drying process system for the Modularized sewage of the intelligent environment protection toilet of the present invention.
Fig. 3 is the schematic perspective view for centrifuging drier of the invention.
Fig. 4 is the sectional view for centrifuging drier of the invention.
Embodiment
Referring to Fig. 1 and Fig. 2, the Modularized sewage separation drying process system of the intelligent environment protection toilet provided in figure, bag
Include module framework 100, collecting box 200, dry powder collecting box 300, centrifugation drier 400, heat exchanger 500, steam separation
Device 600, jet mixer 700, photocatalyst device 800, heater 900, air cleaner 1000 and blower fan 1100.Its
In, collecting box 200, dry powder collecting box 300, centrifugation drier 400, heat exchanger 500, steam trap 600, jet are mixed
Clutch 700, photocatalyst device 800, heater 900, air cleaner 1000 and blower fan 1100 are integrated in module framework 100
It is interior, so it is easy to integral demounting to get off maintenance.
The vacuum sewage system connection that collecting box 200 is connected with intelligent environment protection toilet is arranged to collect intelligent environment protection toilet
The excrement gone out, the collecting box 200 also has a dirt outlet 210, an exhaust outlet 220, the first dirt circulation interface 230 and the
Two dirt circulation interfaces 240.
There is dry powder collecting box 300 dry powder to collect the dry powder discharging opening 320 of import 310 and one, dry powder collecting box 300 it is dry
Powder discharging opening 320 is connected with outside dry powder collection device.
Centrifuge and dirt entrance 410, high-temperature gas entrance 420, dry powder outlet 430 are provided with drier 400 and is given up
Liquid outlet 440, the dirt entrance 410 centrifuged on drier 400 passes through pipeline, blowdown valve group, sewage pump P2 and collecting box
Dirt outlet 210 on 200 is connected, and import 310 is collected in dry powder outlet 430 by the dry powder of pipeline and dry powder collecting box 300
Connection.Blowdown valve group includes the Stress control blowoff valve 450 and manual blowdown valve 460 of parallel connection, wherein Stress control blowoff valve 450
By the Stress control centrifuged in drier 400.
There is first medium entrance 510, first medium outlet 520, second medium entrance 530, second on heat exchanger 500
First medium entrance 510 on media outlet 540, heat exchanger 500 is gone out by pipeline with centrifuging the waste liquid of drier 400
Mouth 440 is connected, and the second medium entrance 530 on heat exchanger 500 is connected with the first dirt circulation interface 230 of collecting box, heat
Second medium outlet 540 on exchanger 500 is connected with the second dirt circulation interface 240 of collecting box 200.
There is a water inlet 610, a gas vent 620 and a water out 630, steam trap on steam trap 600
Water inlet 610 on 600 is connected by pipeline with the first medium outlet 520 on heat exchanger 500, on steam trap 600
Water out 610 pass through draining valve 640 and pipeline and connect water treatment facilities (not shown).
There is a gas access 710, the air intake 730 of gas vent 720 and one, jet mixing on jet mixer 700
Gas access 710 on device 700 is connected by pipeline with the gas vent 620 on steam trap 600, jet mixer 700
On air intake 710 be connected by air shut-off valve group with an air cleaner 1000.Have one on air cleaner 1000
Air intake 1010, air intake 1010 connects an air compressor machine (not shown) by pipeline.Air shut-off valve group is included simultaneously
The magnetic valve 740 and hand-operated valve 750 of connection.
Photocatalyst device 800 is provided with the gas on a gas access 810 and a gas vent 820, photocatalyst device 800
Entrance 810 is connected by pipeline with the gas vent 720 on jet mixer 700.
There is heater 900 cold wind on high-temperature gas outlet 910 and a cold wind import 920, heater 900 to enter
Mouth 920 is connected by pipeline and a blower fan 1100 with the gas vent 820 on photocatalyst device 800, the height on heater 900
Warm gas vent 910 is connected by pipeline with centrifuging the high-temperature gas entrance 420 on drier 400.
The operation principle of the present invention is as follows：
Fecal sewage in collecting box 200 is discharged into centrifugation drier 400 by sewage pump and blowdown valve group to be carried out
Separation of solid and liquid, centrifuges drier 400 in centrifugal separation processes, the High Temperature Gas style being blown into by high-temperature gas entrance 220
Such as on the one hand steam carry out high temperature sterilization to the fecal sewage centrifuged in drier 400, on the other hand and to centrifuging
Solid in drier 400 is dried, and forms dry powder discharge.The water that centrifugation drier 400 is isolated enters heat exchange
In device 500, with the fecal sewage progress heat exchange cooling brought by collecting box 200, the feeding steam trap 600 after cooling
Middle progress steam separation, the water after separation is discharged into water treatment facilities by draining valve 640 further to be handled.The gas isolated
After being mixed by jet mixer 700 with air, sterilized in feeding photocatalyst device 800, the gas after sterilization passes through wind
High-temperature gas is heated into the feeding heater 900 of machine 1100, the high-temperature gas feeding of heating is centrifuged in drier.
The Modularized sewage separation drying process system throughput of the intelligent environment protection toilet of the present invention is big, and in solid-liquid point
From when, to dirt carry out high temperature sterilization so that sewage being capable of reuse.
Referring to Fig. 3 and Fig. 4, centrifuging drier 400 includes a shell 4100, and the shell 4100 is by centrifuging machine support
4110 supports, a high-temperature gas entrance 4120 is provided with the centre position of side face one of shell 4100 (with the label 420 in Fig. 2
Unanimously) and an observation window 4170, a tapping chamber 4130 is provided with the right side of shell 4100, is set in the cavity wall of tapping chamber 4130
It is equipped with a dry powder and exports 4140 (consistent with the label 430 in Fig. 2).
Centrifuge the centrifugal network cylinder assembly 4200 in drier 400 and fixed including net cartridge unit with net cartridge unit two ends and connected
The left and right rotating shaft 4210,4220 connect, left and right rotating shaft 4210,4220 is supported on shell by left and right bearing 4230,4240 respectively
On 4100 left and right side plate 4150,4160, left and right rotating shaft 4210,4220 is hollow rotating shaft.
Net cartridge unit is divided into Intranet cylinder 4250, middle net cylinder 4260 and outer net cylinder 4270, in Intranet cylinder 4250, middle net cylinder 4260
Some meshes 4251,4261,4271 are provided with all barrels of outer net cylinder 4270 and in Intranet cylinder 4250, middle net cylinder 4260
Biological ventilated membrane 4252,4262,4272 is pasted with all barrel inner surfaces of outer net cylinder 4270.
Scum hole 4253 is provided with the right side of all barrels of Intranet cylinder 4250, is set on the left of all barrels of middle net cylinder 4260
Scum hole 4263 is equipped with, scum hole 4273 is provided with the right side end wall of outer net cylinder 4270；The barrel chamber of Intranet cylinder 4250 passes through
Scum hole 4253 is connected with the barrel chamber of middle net cylinder 4260, and the barrel chamber of middle net cylinder 4260 passes through scum hole 4263 and outer net cylinder 4270
Barrel chamber is connected, and the barrel chamber of outer net cylinder 4270 is connected by scum hole 4273 with tapping chamber 4130.Left rotary shaft 4310 and centrifugal network cylinder
Drive device (not shown) drive connection.
One scraper plate 4280 is installed on the right side of net cartridge unit, scraper plate 4280 is located in tapping chamber 4130 and follows net cylinder portion
Part rotate, be circumferentially evenly equipped with scraper plate 4280 it is some scrape pawl 4281, the inner surface for scraping pawl 4281 with tapping chamber 4130 is contacted.
The auger cylinder 4310 of centrifugation drier 400 is located at the left-hand rotation in centrifugal network cylinder assembly by the axle of bearing 4320
In axle 4210, in the barrel chamber of the right-hand member insertion Intranet cylinder 4250 of the auger cylinder 4310, left end stretches out the left plate of shell 4100
4150, a dirt entrance 4311 (consistent with the label 410 in Fig. 2) is offered on the barrel of the left end of auger cylinder 4310,
A waste liquid outlet 4312 (consistent with the label 440 in figure 2) is offered on the barrel of right-hand member, dirt entrance 4312 passes through auger
The inner chamber of cylinder 4310 is connected with waste liquid outlet 4312.
A feeding auger 4320 is rotatablely equipped with auger cylinder 4310, the feeding auger 4320 includes a screw-conveyer-shaft
4321 and one spiral way be fixed in packing auger blade 4322 on screw-conveyer-shaft 4321, screw-conveyer-shaft 4321 it is whole provided with axially penetrating through
The axial bore 4321a of screw-conveyer-shaft 4321, radial direction limbers 4321b, radial direction limbers are offered in the left end of screw-conveyer-shaft 4321
4321b is connected with the axial bore 4321a in screw-conveyer-shaft 4321.
The connector drum 4330 in drier 400 is centrifuged, right-hand member and the auger cylinder 4310 of connector drum 4330 are consolidated
Fixed connection, left end is connected with a reducing gear 4340, and the left end of screw-conveyer-shaft 4310 is supported on connector drum by bearing 4370
In 4330 and through the output shaft drive connection of connector drum 4330 and reducing gear 4340；On the barrel of connector drum 4330
It is provided with flushing water water inlet pipe 4331, barrel chamber and the left end of screw-conveyer-shaft 4320 that flushing water water inlet pipe 4331 passes through connector drum 4330
Radial direction limbers 4321b connection.The input shaft of reducing gear 4340 and the output shaft drive connection of motor 4350.
A spray equipment 4360 is connected with the right-hand member of screw-conveyer-shaft 4310, the spray equipment 4360 is located at the cylinder of Intranet cylinder 4250
In chamber, it includes a shower 4361 and the spray baffle plate 4362,4363 installed in the left and right two ends of shower 4361, shower
4361 inner chamber 4361a is connected with the axial bore 4321a in screw-conveyer-shaft 4321, is arranged at intervals with shower 4361 some
Spray nozzle 4364.
A water out adapter 4420, water out adapter are provided with by bearing 4410 in right spindle 4220 in net cartridge unit
4420 left end is connected with the barrel chamber of Intranet cylinder 4250, and right-hand member connects an outlet pipe 4430.
When needing that fecal sewage is carried out separating dry, start motor 4350 and centrifugal network cylinder drive device, motor 4350
Screw-conveyer-shaft 4321 is driven to rotate by reducing gear 4340, screw-conveyer-shaft 4321 drives packing auger blade 4322 to rotate, and will be gone out by waste liquid
The fecal sewages that mouth 4312 is sent into auger cylinders 4310 are pushed to the direction of waste liquid outlet 4312 and sent into by waste liquid outlet 4312
In the Intranet cylinder 4250 of net cartridge unit.Net cartridge unit high-speed rotation under centrifugal network cylinder drive device driving.High-speed rotation it is interior
Centrifugal force produced by net cylinder 4250 gets rid of the solid in fecal sewage on the biological ventilated membrane 4252 of Intranet cylinder 4250, makes solid
Body is dehydrated for the first time with liquid, and the solid got rid of on the biological ventilated membrane 4252 of Intranet cylinder 4250 is flowed to along biological ventilated membrane 4252
Scum hole 4253, is then flowed into the barrel chamber of middle net cylinder 4260 by scum hole 4253.Because middle net cylinder 4260 also turns at a high speed
Dynamic, the solid in the barrel chamber of net cylinder 4260 in entrance is carried out second and is dehydrated by produced centrifugal force, is dehydrated by second
Solid afterwards flows to scum hole by the biological ventilated membrane 4262 in solid edge got rid of on the biological ventilated membrane 4262 of middle net cylinder 4260
4263, then it is flowed into by scum hole 4263 in the barrel chamber of outer net cylinder 4270, water is then back to along Intranet 4250 outer walls of cylinder
Scum hole 4253 enters in the barrel chamber of Intranet cylinder 4250.Due to outer net cylinder 4270 also high-speed rotation, produced centrifugal force will enter
The solid entered in the barrel chamber of outer net cylinder 4270 carries out third time dehydration, and the solid after third time is dehydrated is got rid of in outer net cylinder
Solid on 4270 biological ventilated membrane 4272 flows to scum hole 4273 along biological ventilated membrane 4272, then passes through scum hole 4273
It is flowed into tapping chamber 4130, water is then back to the barrel chamber of net cylinder 4260 during scum hole 4263 enters along the middle outer wall of net cylinder 4260
In.
Dry slag in tapping chamber 4130 is scraped to dry powder outlet 4140 and is sent to dry by the pawl 4281 of scraping on scraper plate 4280
In powder collecting box 300.
The sewage converged in Intranet 4250 barrel chambers of cylinder is sent at a water by water out adapter 4420 and outlet pipe 4430
Handled in reason device.
Above-mentioned centrifugal network cylinder is in fecal sewage centrifugal separation processes, and high-temperature steam passes through the High Temperature Gas on shell 4100
Body entrance 4120 enters in shell 4100, and further passes sequentially through the mesh 4271 on outer net cylinder 4270 through biological ventilated membrane
4272 enter in 4270 inner chambers of outer net cylinder, the mesh 4261 on middle net cylinder 4260 nets cylinder in entering through biological ventilated membrane 4262
Mesh 4251 in 4260 inner chambers, on Intranet cylinder 4250 enters in 4270 inner chambers of Intranet cylinder through biological ventilated membrane 4252.High temperature
The problem of steam has certain flow velocity and is higher, its one side can will stick to biological ventilated membrane 4252,4262,4272 and blow
Fall, on the other hand can carry out high-temperature sterilization to the fecal sewage in centrifugal separation processes.
In addition, the present invention is by setting spray equipment 4360, when in fecal sewage centrifugal separation processes, spray can be passed through
Device sprays into disinfectant and carries out further disinfecting, deodorizing processing to the fecal sewage in centrifugal separation processes, while needing
During maintenance, rinse water can be sprayed by spray equipment 4360 to be had to the inside of centrifugal network cylinder assembly 4200, shell 4100
Effect cleaning, to facilitate operator to repair and change part.
Claims (8)
1. a kind of Modularized sewage separation drying process system of intelligent environment protection toilet, it is characterised in that including：
What one vacuum sewage system being connected with intelligent environment protection toilet was connected is used to collect the excrement that intelligent environment protection toilet is discharged
Collecting box, the collecting box have a dirt outlet, an exhaust outlet, the first dirt circulation interface and the second dirt circulation connect
Mouthful；
There is one dry powder collecting box, the dry powder collecting box dry powder to collect import and a dry powder discharging opening, and the dry powder is collected
The dry powder discharging opening of case is connected with outside dry powder collection device；
One centrifuges drier, a dirt entrance is provided with the centrifugation drier, a high-temperature gas entrance, one dry
Powder is exported and a waste liquid outlet, and the dirt entrance on the centrifugation drier passes through pipeline, blowdown valve group, sewage pump and institute
State the dirt outlet connection on collecting box；The dry powder outlet import is collected by the dry powder of pipeline and the dry powder collecting box
Connection；
There is first medium entrance, first medium outlet, second medium entrance, second on one heat exchanger, the heat exchanger
First medium entrance on media outlet, the heat exchanger is connected by the waste liquid outlet of pipeline and the centrifugation drier
Connect, the second medium entrance on the heat exchanger is connected with the first dirt circulation interface of the collecting box, the heat exchange
Second medium outlet on device is connected with the second dirt circulation interface of the collecting box；
There is a sewage inlet, a gas vent and an outlet of sewer, the water on one steam trap, the steam trap
Sewage inlet on vapour separator is connected by pipeline with the first medium outlet on the heat exchanger, the steam trap
On outlet of sewer pass through blowoff valve and pipeline and connect water treatment facilities；
There is a gas access, gas vent and an air intake, the jet on one jet mixer, the jet mixer
Gas access on blender is connected by pipeline with the gas vent on the steam trap, on the jet mixer
Air intake is connected by air shut-off valve group with an air cleaner；There is an air intake, institute on the air cleaner
State air intake and one air compressor machine is connected by pipeline；
One photocatalyst device, the photocatalyst device is provided with a gas access and a gas vent, the photocatalyst dress
The gas access put is connected by pipeline with the gas vent on the jet mixer；
One heater, the heater has cold on high-temperature gas outlet and a cold wind import, the heater
Wind inlet is connected by pipeline and a blower fan with the gas vent on the photocatalyst device；High Temperature Gas on the heater
Body outlet is connected by pipeline with the high-temperature gas entrance on the centrifugation drier；And a module framework, the receipts
Header, dry powder collecting box, centrifuge drier, heat exchanger, steam trap, jet mixer, photocatalyst device and
Heater is integrated in the module framework.
2. the Modularized sewage separation drying process system of intelligent environment protection toilet as claimed in claim 1, it is characterised in that
The blowdown valve group includes the Stress control blowoff valve and manual blowdown valve of parallel connection, and wherein Stress control blowoff valve is centrifuged
Stress control in drier.
3. the Modularized sewage separation drying process system of intelligent environment protection toilet as claimed in claim 1, it is characterised in that
The air shut-off valve group includes magnetic valve and hand-operated valve in parallel.
4. the Modularized sewage separation drying process system of intelligent environment protection toilet as claimed any one in claims 1 to 3,
Characterized in that, the centrifugation drier includes：
One shell, the shell is supported by centrifuging machine support, is provided with the centre position of side face one of the shell described in one
High-temperature gas entrance, is provided with a tapping chamber on the right side of the shell, is provided with the cavity wall of the tapping chamber described in one
Dry powder is exported；
One axle sets centrifugal network cylinder assembly in the housing, and the centrifugal network cylinder assembly includes net cartridge unit and the net cylinder portion
The left and right rotating shaft that part two ends are fixedly connected, the left and right rotating shaft is respectively by left and right bearings in the left and right of the shell
On side plate, the left and right rotating shaft is hollow rotating shaft；The net cartridge unit be divided into, in, outer net cylinder, it is described it is interior, in, outer net
Be provided with all barrels of cylinder some meshes and it is described it is interior, in, be pasted with all barrel inner surfaces of outer net cylinder it is biological thoroughly
Air film, it is described in, in, the barrel chamber of outer net cylinder be sequentially communicated, the barrel chamber of outer net cylinder is connected with the tapping chamber；The left-hand rotation
Axle and centrifugal network cylinder drive device drive connection；
One is located at the auger cylinder in the left rotary shaft in the centrifugal network cylinder assembly, the right-hand member of the auger cylinder by bearing axle
In the barrel chamber for inserting the Intranet cylinder, the left end of the auger cylinder stretches out the shell, in the cylinder of the auger cylinder left end
Dirt entrance described in one is offered on wall, waste liquid outlet described in one is offered on the barrel of the auger cylinder right-hand member, it is described
Dirt entrance is connected by the auger cylinder lumen with the waste liquid outlet；
One is rotatably installed in the feeding auger in the auger cylinder lumen, and the feeding auger includes a screw-conveyer-shaft and a spiral
Mode is fixed on the axial bore being provided with the packing auger blade on the screw-conveyer-shaft, the screw-conveyer-shaft through the screw-conveyer-shaft,
The left end of the screw-conveyer-shaft offers radial direction limbers, and the radial direction limbers is connected with the axial bore in the screw-conveyer-shaft；
One connector drum, the right-hand member of the connector drum is fixedly connected with the auger cylinder, and left end is connected with a reducing gear,
The left end of the screw-conveyer-shaft is by bearings in the connector drum and through the connector drum and the reducing gear
Output shaft drive connection；Flushing water water inlet pipe is provided with the barrel of the connector drum, the flushing water water inlet pipe leads to
The barrel chamber for crossing the connector drum is connected with the radial direction limbers of the screw-conveyer-shaft left end；
One motor being connected with the reducing gear, the input shaft driving of the output shaft of the motor and the reducing gear connects
Connect；
One spray equipment for being connected and being located in the Intranet cylinder barrel chamber with the screw-conveyer-shaft right-hand member；
One is arranged on the water out adapter in the right spindle in the net cartridge unit, the left end of the water out adapter and institute by bearing
The barrel chamber connection of Intranet cylinder is stated, the right-hand member of the water out adapter connects an outlet pipe.
5. the Modularized sewage separation drying process system of intelligent environment protection toilet as claimed in claim 4, it is characterised in that
The spray equipment includes a shower and installed in the shower is left, the spray baffle plate by two ends, the shower it is interior
Chamber is connected with the axial bore in the screw-conveyer-shaft, and some spray nozzles are arranged at intervals with the shower.
6. the Modularized sewage separation drying process system of intelligent environment protection toilet as claimed in claim 4, it is characterised in that
The first scum hole is provided with the right side of all barrels of Intranet cylinder, second is provided with the left of all barrels of the middle net cylinder
Scum hole, the 3rd scum hole is provided with the right side end wall of outer net cylinder；The barrel chamber of the Intranet cylinder passes through described first
Scum hole is connected with the barrel chamber of the middle net cylinder, and the barrel chamber of the middle net cylinder passes through second scum hole and outer net cylinder
Barrel chamber is connected, and the barrel chamber of the outer net cylinder is connected by the 3rd scum hole with the tapping chamber.
7. the Modularized sewage separation drying process system of intelligent environment protection toilet as claimed in claim 4, it is characterised in that
An observation window is provided with the side face of the shell.
8. the Modularized sewage separation drying process system of intelligent environment protection toilet as claimed in claim 4, it is characterised in that
One scraper plate is installed on the right side of the net cartridge unit, the scraper plate is located in the tapping chamber, it is circumferential equal on the scraper plate
Be furnished with it is some scrape pawl, the pawl of scraping is contacted with the inner surface of the tapping chamber.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201710589794.3A CN107265820B (en) | 2017-07-19 | 2017-07-19 | Modularization filth separation drying process system that intelligence environmental protection lavatory was used |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201710589794.3A CN107265820B (en) | 2017-07-19 | 2017-07-19 | Modularization filth separation drying process system that intelligence environmental protection lavatory was used |
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| Publication Number | Publication Date |
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| CN107265820A true CN107265820A (en) | 2017-10-20 |
| CN107265820B CN107265820B (en) | 2020-10-30 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201710589794.3A Expired - Fee Related CN107265820B (en) | 2017-07-19 | 2017-07-19 | Modularization filth separation drying process system that intelligence environmental protection lavatory was used |
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| CN108739418A (en) * | 2018-04-12 | 2018-11-06 | 曾碧阳 | A kind of rabbit breeding apparatus of the herding convenient for cleaning |
| CN108947138A (en) * | 2018-08-08 | 2018-12-07 | 张家港市欧微自动化研发有限公司 | A kind of sewage disposal device |
| CN108975618A (en) * | 2018-08-08 | 2018-12-11 | 张家港市欧微自动化研发有限公司 | A kind of sewage water treatment method based on sewage disposal device |
| CN109896719A (en) * | 2019-03-13 | 2019-06-18 | 王惟 | A kind of the environmental protection treatment device and its processing method of excrement blowdown |
| CN109970141A (en) * | 2019-04-29 | 2019-07-05 | 江苏旭云物联信息科技有限公司 | A kind of water polluting matter automation quick treatment device suitable for Mobile Equipment |
| CN110255771A (en) * | 2019-07-03 | 2019-09-20 | 东莞市宇科机械科技有限公司 | Deodorization equipment for urban road sewage treatment and working method thereof |
| CN113548912A (en) * | 2021-07-16 | 2021-10-26 | 夏能文 | The solid-liquid separation and reuse in buildings and municipal pipelines are converted into high-efficiency organic fertilizer systems |
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| CN201309444Y (en) * | 2008-09-02 | 2009-09-16 | 张迎秋 | Excrement rapid drying environmental sanitation disposal vehicle |
| CN106149831A (en) * | 2015-04-20 | 2016-11-23 | 国涟建设集团有限公司 | Toilet feces collector |
| CN106747691A (en) * | 2015-11-25 | 2017-05-31 | 江苏科化节能环保设备有限公司 | One kind cultivation soiled litter sterilizing and drying integral type disposing technique and system |
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| CN201309444Y (en) * | 2008-09-02 | 2009-09-16 | 张迎秋 | Excrement rapid drying environmental sanitation disposal vehicle |
| CN106149831A (en) * | 2015-04-20 | 2016-11-23 | 国涟建设集团有限公司 | Toilet feces collector |
| CN106747691A (en) * | 2015-11-25 | 2017-05-31 | 江苏科化节能环保设备有限公司 | One kind cultivation soiled litter sterilizing and drying integral type disposing technique and system |
Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108739418A (en) * | 2018-04-12 | 2018-11-06 | 曾碧阳 | A kind of rabbit breeding apparatus of the herding convenient for cleaning |
| CN108739418B (en) * | 2018-04-12 | 2020-08-28 | 绍兴大纬针织机械有限公司 | Poultry is with rabbit feeding device convenient to wash |
| CN108947138A (en) * | 2018-08-08 | 2018-12-07 | 张家港市欧微自动化研发有限公司 | A kind of sewage disposal device |
| CN108975618A (en) * | 2018-08-08 | 2018-12-11 | 张家港市欧微自动化研发有限公司 | A kind of sewage water treatment method based on sewage disposal device |
| CN109896719A (en) * | 2019-03-13 | 2019-06-18 | 王惟 | A kind of the environmental protection treatment device and its processing method of excrement blowdown |
| CN109970141A (en) * | 2019-04-29 | 2019-07-05 | 江苏旭云物联信息科技有限公司 | A kind of water polluting matter automation quick treatment device suitable for Mobile Equipment |
| CN110255771A (en) * | 2019-07-03 | 2019-09-20 | 东莞市宇科机械科技有限公司 | Deodorization equipment for urban road sewage treatment and working method thereof |
| CN113548912A (en) * | 2021-07-16 | 2021-10-26 | 夏能文 | The solid-liquid separation and reuse in buildings and municipal pipelines are converted into high-efficiency organic fertilizer systems |
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|---|---|
| CN107265820B (en) | 2020-10-30 |
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Effective date of registration: 20230726 Address after: 201306 room 9045, area 1, building 1, No. 888, Huanhu West 2nd Road, Nanhui new town, Pudong New Area, Shanghai Patentee after: SHANGHAI XIANGER PANRONG ENVIRONMENTAL PROTECTION ENERGY SAVING TECHNOLOGY Co.,Ltd. Address before: Room a-b102-659, 198 Qidi Road, Xiaoshan Economic and Technological Development Zone, Hangzhou, Zhejiang 311200 Patentee before: HANGZHOU SHANGHANG TECHNOLOGY Co.,Ltd. |
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