CN107265769A - Intelligent environment protection toilet is without emissions and recycles automated programming system - Google Patents
Intelligent environment protection toilet is without emissions and recycles automated programming system Download PDFInfo
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- CN107265769A CN107265769A CN201710579273.XA CN201710579273A CN107265769A CN 107265769 A CN107265769 A CN 107265769A CN 201710579273 A CN201710579273 A CN 201710579273A CN 107265769 A CN107265769 A CN 107265769A
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- 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
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- 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
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- 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
- C02F1/46—Treatment of water, waste water, or sewage by electrochemical methods
- C02F1/461—Treatment of water, waste water, or sewage by electrochemical methods by electrolysis
- C02F1/46104—Devices therefor; Their operating or servicing
-
- 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
- C02F1/00—Treatment of water, waste water, or sewage
- C02F2001/007—Processes including a sedimentation step
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- 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
Abstract
The present invention intelligent environment protection toilet is without emissions and recycles automated programming system, including：Intelligent environment protection toilet, vacuum sewage system, the first ejector, the first collecting box, the second collecting box, the second ejector, solid-liquid separator, drying system, the first baffle-box, the first self priming pump, precipitation buffering case, electrolysis unit, membrane cisterna, ozone generator, elevated tank and control device.The present invention intelligent environment protection toilet is without emissions and recycles automated programming system automatic running, without operating personnel's operation, whole processing procedure is physical treatment course, without chemical reagent, dry powder after processing can be used as lavatory water as fertilizer, the water of processing.The intelligent environment protection toilet of the present invention is without emissions and recycles automated programming system and can be used for various places, without laying drainage pipeline in addition, reduces the investment of lavatory.
Description
Technical field
The present invention relates to stool detection technical field, more particularly to intelligent environment protection toilet is without emissions and circulation
Utilize automated programming system.
Background technology
Population increase and high concentration is so that the yield of urban night soil is continuously increased, these excrement are in past most conduct
Fertilizer directly transports rural area to, and at present in the case where that can bring the impact of chemical fertilizer of distinct economic, excrement makes rural area
Consumption increasingly atrophy.Thus, excrement is managed using suitable technology not only has great with handling to environmental protection
Meaning, and to ensureing that the health of the people also has profound significance.
Excrement and urine water mainly has high suspended particulate substance (SS), ammonia nitrogen (NH3-N) concentration height, organic matter (COD) concentration is high, feel
The features such as official's degree is poor, biodegradability is good.Have at present for the main treatment technology of excrement and urine water：It is anaerobic fermentation facture, aerobic
Facture, high temperature high pressure process method, septic tank facture, materialization treatment process, During High-Temperature Composting method etc., but the country is in reality at present
The stool detection technology being most widely used in engineering is broadly divided into two classes：
One class：Septic tank processing:In small and medium-sized cities and rural area due to the processing of sanitary sewage, collecting dung, processing are complete
Pipelineization is relatively difficult, and small-sized septic tank just turns into the facility that apartment is most universal and must configure.The function of septic tank is
Receive, store family domestic sewage.It is divided into floating layer, mud and middle 3 region of clear water layer in pond.Clear water can use sewage
The mode of irrigation makees final process.Current widely using due to chemical products, the composition of family domestic sewage is increasingly sophisticated, dirty
Harmful substance contents increase in water, the direct discharge of septic tank " clear water layer " just turns into the pollution sources in sewage irrigation region.To this
The control for planting pollution is only to decompose to precipitate harmful substance using a large amount of chemicalses in septic tank, but is filled expanding sewage
Region is irrigate, increase soil treatment is functionally to be difficult to effectively.While septic tank processing is also easy to, appearance is blocked, spoil disposal is difficult,
Handle the problems such as thorough, mosquitos and flies does not grow.
Two classes：Materializing strategy:It is 200710079587 in China Patent No..X, publication date are September in 2007 19 days, title
A kind of method of materializing strategy excrement disclosed in patent document for " dejecta treatment method and system ".This method is to pass through solid-liquid
Excrement is carried out separation of solid and liquid by separation equipment, and the residue isolated carries out landfill disposal, and the liquid manure isolated adds appropriate chemistry
Medicament, makes liquid manure occur by dehydration equipment progress dewater treatment after flocculation, wherein dry clay as fertile obtained by dehydration
Material, liquid deliver to sewage treatment plant and carry out terminal processes.The dejecta treatment method of above pattern has the following disadvantages：For highly concentrated
Spend being received for organic fecal sewage, it is desirable to which the condition such as designed capacity, operating mode of sewage treatment plant meets by receiving the standard of sewage, and
Fecal sewage is that randomness is discharged into sewage network, and the construction plan to sewage treatment plant brings very big inconvenience；Fecal sewage is defeated
Dense stink can be given out and be difficult to handle stink by being sent in the way of sewage treatment plant, be unfavorable for environmental sanitation.
In order to solve the not enough above of above type of dejecta treatment method, it have devised to liquid dung produced after dehydration
It is further processed to reach the stool detection method discharged again after discharge mark.It is in Chinese Patent Application No.
201210251613.3rd, publication date is on October 24th, 2012, entitled " a kind of decontamination of human excreta recycling processing method "
Switched in patent document it is a kind of can be by the method for the liquid waste processing in excrement to qualified discharge.This method is gained after being dehydrated
Waste liquid carry out gathering chelation treatment and oxygen processing successively and one-level/bis- grade Aerobic Process for Treatment is discharged afterwards to up to standard.The type
Processing method have the following disadvantages：Directly waste liquid is carried out successively to gather chelation treatment and oxygen processing and one-level/bis- grade are aerobic
Handle it is up to standard after discharged, the processing method causes the organic matter for making nutrient in liquid dung to be decomposed into can not be as nutrient
Organic matter, it is impossible to realize abundant recycling to the organic matter in excrement and nitrogen treatment not thoroughly, COD removal efficiency
It is low；The dewater treatment of sludge and excrement is carried out together by same centrifuge, the reasonable utilization for the nutrient being not easy in excrement, because
For excrement be dehydrated obtained by dry mud nutrient it is high, can be used as fertilizer and be used, and the dry mud obtained by sludge dewatering does not almost have
What nutrient is improper as fertilizer utilization.
For the deficiency of above-mentioned technology, Chinese patent Authorization Notice No. CN103073149B discloses a kind of decontamination of human excreta
Processing method, it is handled excrement in accordance with the following steps：
1st step, by solid-liquid separating machine to excrement carry out separation of solid and liquid；
It is dehydrated after 2nd step, the liquid flocculation for isolating the 1st step by centrifuge；
3rd step, by the liquid isolated in the 2nd step in anaerobic digester by the effect of anaerobe, make waste water
In organic matter decomposition and inversion turn into after methane and carbon dioxide mud-water separation carried out by the method for precipitation；
4th step, by the liquid isolated in the 3rd step carry out denitrogenation processing；
Denitrogenation processing comprises the following steps：
4-1 is walked, is adjusted the pH value for the liquid isolated in the 3rd step to 9.5~12；
4-2 is walked, the method that the liquid produced in 4-1 steps is taken off by air-blowing is made into the free ammonia volatilization in liquid, so
The ammonia volatilized is absorbed with acid solution afterwards and ammonium salt is generated；
4-3 is walked, the liquid after walking denitrogenation through 4-2 is carried out into neutralisation treatment, by pH value regulation to 7.5~8.5；
5th step, the liquid after the 4th step denitrogenation processing is subjected to degraded COD, BOD and ammonia nitrogen；
5-1 step, by the liquid after the 4th step denitrogenation be transported in one-level anoxic pond handle after be transported to one-level Aerobic Pond again
It is middle to be handled；Anaerobic bacteria in one-level anoxic pond makes the larger molecular organicses in liquid be degraded to small organic molecule, anti-
Nitrobacteria is carried out instead using the organic matter in liquid for the mixed liquor containing nitrate nitrogen flowed back in carbon source and one-level Aerobic Pond
Nitration reaction, nitrogen is converted into by the nitrate nitrogen in water；Aerobic bacteria in one-level Aerobic Pond is under Effect of Dissolved Oxygen by liquid
Middle organic matter, which absorbs, to be decomposed, and is converted into CO2 and itself organic matter, and Simultaneous Nitrification bacterium is also by the ammonium oxidation in water into nitre state
Nitrogen；
5-2 steps, the liquid after the processing of one-level Aerobic Pond are transported to after being handled in two grades of anoxic ponds is transported to two grades again
Handled in Aerobic Pond；It is organic that anaerobic bacteria in two grades of anoxic ponds makes the larger molecular organicses in liquid be degraded to small molecule
Thing, denitrifying bacteria are entered using the organic matter in liquid for the mixed liquor containing nitrate nitrogen flowed back in carbon source and two grades of Aerobic Ponds
Row anti-nitration reaction, nitrogen is converted into by the nitrate nitrogen in water；Aerobic bacteria in two grades of Aerobic Ponds will under Effect of Dissolved Oxygen
Organic matter, which absorbs, in liquid decomposes, and is converted into CO2 and itself organic matter, Simultaneous Nitrification bacterium also by the ammonium oxidation in water into
Nitrate nitrogen；Liquid after two grades of Aerobic Pond processing, which is transported in the 6th step, to be handled.
6th step, the method progress mud-water separation that the liquid after being handled through the 5th step is passed through into precipitation；
7th step, the liquid for isolating the 6th step carry out disinfection processing after discharge.
8th step, the sludge dewatering in dewater treatment, the 8th step and the 2nd step are carried out by the sludge produced in the 3rd step and the 6th step
In the dehydrate liquids for isolating the 1st step separately carry out.
The core of the patent and be to carry out denitrogenation processing to ammonia nitrogen by stripping method a little, denitrogenation processing efficiency high enters
Enter to carry out degraded COD, BOD and ammonia nitrogen so that CODCr≤450mg/L in the waste water of discharge, SS≤350mg/L, BOD5≤
250mg/L, NH3-N≤28mg/L；Discharge before disinfected, make pathogen therein, parasitic ovum and fly maggot go out extremely,
Reach harmless in health；Methane and ammonium salt will be isolated in excrement in processing, the utilization to the organic matter in excrement is abundant.But
The shortcoming for being the patent is that the operation of whole system needs operating personnel's control, additionally needs and delivers some chemical reagent, once
Chemical reagent is delivered excessively, is made troubles to subsequent treatment.
The content of the invention
The technical problems to be solved by the invention are that many technologies present in above-mentioned stool detection are asked
Inscribe and a kind of automatic operating is provided, the intelligent environment protection toilet of chemical reagent need not be delivered without emissions and recycled automatic
Change processing system.
The technical problems to be solved by the invention can be realized by following technical solution：
Intelligent environment protection toilet is without emissions and recycles automated programming system, including：
One vacuum sewage system being connected with intelligent environment protection toilet, the vacuum sewage system is to collect intelligent environment protection lavatory
The excrement discharged；
There is an entrance and an outlet and an ozone supply mouthful on one first ejector, first ejector, it is described
The outlet of the entrance of first ejector and the vacuum sewage system is by being connected；
One first collecting box, the entrance of first collecting box is connected with the outlet of first ejector by pipeline；
One second collecting box, the entrance of second collecting box by pipeline and the first collecting box blowoff valve, flowmeter with
The floss hole connection of first collecting box；
There is an entrance and an outlet and an ozone supply mouthful on one second ejector, second ejector, it is described
The floss hole of the entrance of second ejector and second collecting box is by being connected；
There is one solid-liquid separator, the solid-liquid separator solidliquid mixture entrance, one to separate liquid outlet and one point
From aqueous solid outlet, the solidliquid mixture entrance of the solid-liquid separator is penetrated by the second collecting box blowoff valve with described second
Flow the outlet connection of device；
There is one drying system, the drying system separation aqueous solid entrance, dry powder outlet and a separation water to go out
Mouthful, the separation aqueous solid entrance of the drying system passes through a solid-liquid separator aqueous solid drain valve and the separation of solid and liquid
The separation aqueous solid outlet connection of device；
One first baffle-box, the entrance of first baffle-box separates water discharging valve and the drying by a drying system
The separation water out connection of system；
One first self priming pump, the entrance of first self priming pump by pipeline and solid-liquid separator separate liquid emission valve with
The separation liquid outlet connection of the solid-liquid separator；The outlet of first self priming pump is connected with the entrance of one first threeway；
The entrance of first self priming pump is also connected by pipeline, separation water discharging valve with the separation water out of first baffle-box；
One precipitation buffering case, the precipitation buffering case has an entrance and an outlet, and the entrance of the precipitation buffering case leads to
Piping is connected with the first outlet in first threeway；The outlet of the precipitation buffering case passes through precipitation buffering case blowoff valve
Connect the entrance of a measuring pump；
One electrolysis unit, the electrolysis unit has a liquid inlet and liquid outlet, and the liquid of the electrolysis unit enters
Mouth is connected by measuring pump control valve with the outlet of the measuring pump；
One membrane cisterna, the membrane cisterna is divided into according to water flow direction scrapes slag bath, sedimentation basin, MBP ponds and clear water reserviors, described to scrape slag
The flowing of water is flowed by overflow manner between pond and sedimentation basin, between sedimentation basin and MBP ponds；Described scrape is provided with slag bath
Electrolyte entrance, slag outlet, sewage draining exit, recoil mouth, the electrolyte entrance scraped on slag bath is by being electrolysed hydraulic control valve and institute
The liquid outlet connection in electrolysis unit is stated, the slag scraped on slag bath is exported by control valve and the pipeline and described second of slagging tap
The entrance connection of collecting box, the sewage draining exit scraped on slag bath is by scraping slag bath blowoff valve and pipeline and second collecting box
Entrance connection, the mouth that recoiled on slag bath of scraping passes through the first recoil valve and pipeline and the second outlet in first threeway
Connection；The sedimentation basin has a sewage draining exit and a recoil mouth, and the sewage draining exit of the sedimentation basin passes through sedimentation basin pollution discharge valve and pipe
Road is connected with the entrance of first self priming pump, and the recoil mouthful of the sedimentation basin is connected by pipeline with first recoil valve；
The MBP ponds have a sewage draining exit, an aeration opening, a clear water flow export and a recoil mouth, and the sewage draining exit in the MBP ponds passes through
MBP ponds blowoff valve and pipeline are connected with the entrance of first self priming pump, and the aeration opening in the MBP ponds is exposed by pipeline connection one
Air pump, the clear water flow export in the MBP ponds connects the entrance of one second self priming pump by MBP ponds draining valve；The clear water reserviors tool
There are a water inlet, a cooling water recovery port and a discharge outlet, the water inlet of the clear water reserviors passes through clear water reserviors water intaking valve and pipeline
Outlet with one the 3rd ejector is connected, and the entrance of the 3rd ejector is connected by the outlet of pipeline and second self priming pump
Connect, also there is an ozone supply mouthful on the 3rd ejector；
One ozone generator, the air intake of the ozone generator connects an air compressor machine, the ozone hair by pipeline
The ozone outlet of raw device by pipeline pick out after be divided into three branch roads, wherein first branch road passes through the first ejector ozone control valve
It is connected with the ozone supply mouthful of first ejector, Article 2 branch road passes through the second ejector ozone control valve and described second
The ozone supply of ejector mouthful connection, Article 3 branch road is smelly by the 3rd ejector ozone control valve and the 3rd ejector
Oxygen supply mouthful connection；The entrance of cooling circulating water pump in the ozone generator by cooling water control valve and pipeline with it is described
The outlet of cooling circulating water pump in discharge outlet connection in clear water reserviors, the ozone generator passes through pipeline and the clear water reserviors
In cooling water recovery port connection；
One elevated tank, the elevated tank has a water inlet and a delivery port, and the water inlet of the elevated tank leads to
Cross a booster pump, a water inlet control valve to be connected with the discharge outlet of the clear water reserviors, the delivery port of the elevated tank passes through pipeline
It is divided into four branch roads after picking out, wherein tie point is connected by MBR ponds recoil valve and MBR ponds recoil mouth, to MBR
Recoiled in pond；Second branch road is connected by High Pressure Drain valve with the intelligent environment protection toilet ground flushing system, will be unnecessary
Water high pressure is discharged to rinse ground, and the water after flushing is back in the vacuum sewage system again；3rd branch road is by flushing the toilet
Draining valve is connected with the intelligent environment protection toilet flushing system, to flush the toilet after an action of the bowels；4th branch road is washed one's hands water management by first
Valve and a booster pump are connected with the entrance of a pressure water tank, and the outlet of the pressure water tank is washed one's hands by a pressure switch, second
Water control valve and the intelligent environment protection toilet cell system of washing one's hands are connected；The sewage draining exit of the pressure water tank is arranged by a pressure water tank
Dirty valve and pipeline are connected with the first self priming pump；
One control device, the control device is respectively to above-mentioned vacuum sewage system, the first ejector, first collecting box
It is liquid level, the liquid level of the second collecting box, the first collecting box blowoff valve, flowmeter, the second collecting box blowoff valve, the second ejector, solid
Liquid/gas separator aqueous solid drain valve, the liquid level of the first baffle-box, drying system separation water discharging valve, the first self priming pump, precipitation
Liquid level, precipitation buffering case blowoff valve, measuring pump, electrolysis unit, the liquid level measured pump control valve, scrape slag bath, the precipitation of baffle-box
The liquid level in pond, the liquid level in MBP ponds, the liquid level of clear water reserviors, be electrolysed hydraulic control valve, control valve of slagging tap, scrape slag bath blowoff valve, it is first anti-
Rush valve, sedimentation basin pollution discharge valve, MBP ponds blowoff valve, aeration pump, MBP ponds draining valve, the second self priming pump, clear water reserviors water intaking valve, the 3rd
Ejector, ozone generator, air compressor machine, the first ejector ozone control valve, the second ejector ozone control valve, the 3rd ejector
The liquid level of cooling circulating water pump, elevated tank in ozone control valve, ozone generator, booster pump, water inlet control valve, MBR ponds
Recoil valve, High Pressure Drain valve, draining valve of flushing the toilet, first wash one's hands water control valve, booster pump, the liquid level of pressure water tank, pressure switch,
Second wash one's hands water control valve, pressure water tank blowoff valve connection.
In a preferred embodiment of the invention, it is respectively provided with first collecting box, precipitation buffering case and membrane cisterna
There is the exhaust outlet on exhaust outlet, first collecting box, precipitation buffering case and membrane cisterna to be converged to by pipeline in a filter, so
Emptied afterwards by air-introduced machine.
As a result of technical scheme as above, intelligent environment protection toilet of the invention is without emissions and recycles automatic
Change processing system automatic running, without operating personnel's operation, whole processing procedure is physical treatment course, without chemical reagent,
Dry powder after processing can be used as lavatory water as fertilizer, the water of processing.The intelligent environment protection toilet of the present invention is without dirt
Discharge and recycle automated programming system and can be used for various places, without laying drainage pipeline in addition, reduce lavatory
Investment.
Brief description of the drawings
Fig. 1 be intelligent environment protection toilet of the present invention without emissions and recycle automated programming system principle illustrate
Figure.
Embodiment
Referring to Fig. 1, the intelligent environment protection toilet provided in figure is without emissions and recycles automated programming system, including
One vacuum sewage system 100 being connected with intelligent environment protection toilet, the vacuum sewage system 100 is to collect intelligent environment protection toilet
110 excrement discharged.
The excrement that the vacuum sewage system 100 is collected is entered in a collecting box 120 by an ejector I-15, ejector
Ozone supply mouthful on I-15 is connected to ozone generator 130 by ejector ozone control valve V-146, and ozone is in ejector I-
Mixed in 15 with excrement, first time sterilization is carried out to excrement.
After the excrement in collecting box 120 reaches certain liquid level, collecting box blowoff valve V-1, V-149, collecting box are opened
Excrement in 120 is discharged into collecting box 150 by collecting box blowoff valve V-1, V-149 and electromagnetic dosing pump 140.
After the excrement in collecting box 150 reaches certain liquid level, ejector I-12 and collecting box blowoff valve V- is opened
136, the excrement in collecting box 150 is discharged into solid-liquid separator 160 by the solidliquid mixture entrance of solid-liquid separator 160,
Ozone supply mouthful on ejector I-12 is connected to ozone generator 130 by ejector ozone control valve V-147, and ozone is being penetrated
Mixed in stream device I-12 with excrement, carrying out second to excrement sterilizes.
Solid-liquid separator 160 carries out separation of solid and liquid, the separating liquid that the liquid after separation passes through solid-liquid separator 160 to excrement
Body outlet, solid-liquid separator separation liquid emission valve V-139, self priming pump 170, threeway V-166, the entrance of precipitation buffering case 180
Buffer-precipitation is carried out into precipitation buffering case 180.Separation aqueous solid after solid-liquid separator 160 is separated passes through separation of solid and liquid
The separation for separating aqueous solid outlet, solid-liquid separator aqueous solid drain valve V-148 and drying system 190 of device 160 is aqueous
Solid inlet enters to be dried in drying system 190.
Drying system 190 will separate the dried dry powder of aqueous solid and export collection by the dry powder in drying system 190,
As fertilizer.Drying system 190 will separate the dried separation water of aqueous solid by separating water out, drying system separation water
Drain valve V-144, baffle-box E-64 entrance are discharged into baffle-box E-64.
Separation water liquid level in baffle-box E-64 is reached after certain liquid level, opens separation water discharging valve V-142, baffle-box E-
Separation water in 64 passes through the separation water out of baffle-box, separation water discharging valve V-142, self priming pump 170, threeway V-166, precipitation
The entrance of baffle-box 180, which enters in precipitation buffering case 180, carries out buffer-precipitation.
Mixture in precipitation buffering case 180 passes through precipitation buffering case blowoff valve V-2, measuring pump 200, metering pump control valve
V-3 quantitatively sends into electrolysis unit 210 and is electrolysed.The macromolecular in mixture is resolved into small molecule in electrolytic process.Electricity
Electrolyte after solution enters scraping in slag bath 220 in membrane cisterna by liquid outlet, the electrolysis hydraulic control valve V-4 of electrolysis unit 210.
The slag-scraper scraped in slag bath 220 scrapes off the scum silica frost floated on the surface, in order to avoid the sedimentation basin 230 flowed in membrane cisterna
In.The slag that slag-scraper is scraped out is exported by slag, control valve V-173, V-168 of slagging tap and pipeline are sent in collecting box 150
Re-start processing.Scrape sediment in slag bath 220 by sewage draining exit, scrape slag bath blowoff valve V-5, V-134 and pipeline is sent to
Processing is re-started in collecting box 150.The treated water scraped in slag bath 220 is flowed into sedimentation basin 230 by overflow manner
It is middle to be precipitated.
Water in sedimentation basin 230 is flowed into MBP ponds 240 by overflow manner to be aerated and film process, sedimentation basin 230
In sediment pass through sewage draining exit, MBP ponds blowoff valve V-7, V-152, self priming pump 170, threeway V-166, precipitation buffering case 180
Entrance, which enters in precipitation buffering case 180, carries out buffer-precipitation.
Aeration pump 250 is opened, Air Exposure can be carried out to the water in MBP ponds 240.Precipitating sludge in MBP ponds 240 leads to
Cross sewage draining exit, MBP ponds blowoff valve V-8, V-151, self priming pump 170, threeway V-166, the entrance of precipitation buffering case 180 and enter precipitation
In baffle-box 180.MBP ponds 240 handle after clear water by clear water flow export, MBP ponds draining valve V10, V170, self priming pump 270,
Ejector I-16, clear water reserviors water intaking valve V-9, the water inlet of clear water reserviors 260 enter clear water reserviors 290.Ozone on ejector I-16
Supply mouth is connected to ozone generator 130 by ejector ozone control valve V-132, and ozone is carried out in ejector I-16 with water
Mixing, is sterilized to water.
Water in clear water reserviors 260 can be delivered in ozone generator 130 by cooling water control valve V-150 and pipeline, right
Ozone generator 130 is cooled down, and the water after cooling is back in clear water reserviors 260 by cooling circulating water pump 131 and pipeline.Separately
Clear water in outer clear water reserviors 260 can also send into high-pressure water tank E-51 storages by water inlet control valve V-125, booster pump 280.
Ozone generator 130 is connected with air compressor machine 310.
It is clear in MBR pond recoil valve V-171, high-pressure water tank E-51 if necessary to when being recoiled to MBP ponds 240, start
Water recoils to MBR ponds 240.Clear water in other high-pressure water tank E-51 can be sent by High Pressure Drain valve V-133 and pipeline
To the ground flushing system of intelligent environment protection toilet 110, unnecessary water high pressure is discharged to rinse ground, the water after flushing is returned again
It flow in vacuum sewage system 100；Clear water in high-pressure water tank E-51 can also deliver to intelligent ring by the draining valve V-145 that flushes the toilet
The flushing system of lavatory 110 is protected, to flush the toilet after an action of the bowels；Clear water in high-pressure water tank E-51 can also also pass through water control valve of washing one's hands
V-126, booster pump 290 send into a pressure water tank E-60, and pressure water tank E-60 water passes through a pressure switch 300, water control of washing one's hands
Valve V-138 processed delivers to the cell system of washing one's hands of intelligent environment protection toilet 110；The sludge of pressure water tank E-60 depositions is arranged by pressure water tank
Dirty valve V-137, self priming pump 170, threeway V-166, the entrance of precipitation buffering case 180 enter in precipitation buffering case 180
Exhaust outlet, collecting box 120, precipitation buffering case are provided with collecting box 120, precipitation buffering case 180 and membrane cisterna
180 and membrane cisterna on exhaust outlet converged to by pipeline in a filter E-50, then emptied by air-introduced machine E-49.
Intelligent environment protection toilet is without emissions and recycles the control device in automated programming system and (does not show in figure
Go out) respectively to vacuum sewage system 100, ejector I-15, I-12, I-16, the liquid level of collecting box 120,150, collecting box blowdown
It is valve V-1, V-149, V-136, flowmeter 140, solid-liquid separator aqueous solid drain valve V-148, baffle-box E-64 liquid level, dry
Drying system separation water discharging valve V-144, self priming pump 170,270, the liquid level of precipitation buffering case 180, precipitation buffering case blowoff valve V-
2nd, measuring pump 200, electrolysis unit 210, metering pump control valve V-3, the liquid level for scraping slag bath 220, the liquid level of sedimentation basin 230, MBP ponds
240 liquid level, the liquid level of clear water reserviors 260, electrolysis hydraulic control valve V-4, control valve of slagging tap V-173, V-168, scrape slag bath blowoff valve
V-5, V-134, recoil valve V-6, sedimentation basin pollution discharge valve V-7, V-152, MBP pond blowoff valve V-8, V-151, aeration pump 250, MBP
Pond draining valve V-10, V-170, clear water reserviors water intaking valve V-9, ozone generator 130, air compressor machine 310, ejector ozone control valve V-
146th, in V-147, V-132, ozone generator 130 cooling circulating water pump 131, elevated tank E-51 liquid level, booster pump
280th, 290, water inlet control valve V-125, MBR ponds recoil valve V-171, High Pressure Drain valve V-133, the draining valve V-145 that flushes the toilet, wash one's hands
Water control valve V126, pressure water tank E-60 liquid level, pressure switch 300, the water control valve V-138 that washes one's hands, pressure water tank blowoff valve
They are controlled by V-137, air-introduced machine E-49 connections.
Claims (2)
1. intelligent environment protection toilet is without emissions and recycles automated programming system, it is characterised in that including：
One vacuum sewage system being connected with intelligent environment protection toilet, the vacuum sewage system is to collect intelligent environment protection toilet institute
The excrement of discharge；
There is an entrance and an outlet and an ozone supply mouthful, described first on one first ejector, first ejector
The outlet of the entrance of ejector and the vacuum sewage system is by being connected；
One first collecting box, the entrance of first collecting box is connected with the outlet of first ejector by pipeline；
One second collecting box, the entrance of second collecting box by pipeline and the first collecting box blowoff valve, flowmeter with it is described
The floss hole connection of first collecting box；
There is an entrance and an outlet and an ozone supply mouthful, described second on one second ejector, second ejector
The floss hole of the entrance of ejector and second collecting box is by being connected；
There is one solid-liquid separator, the solid-liquid separator solidliquid mixture entrance, a separation liquid outlet and a separation to contain
Water solid is exported, and the solidliquid mixture entrance of the solid-liquid separator passes through the second collecting box blowoff valve and second ejector
Outlet connection；
One drying system, the drying system has a separation aqueous solid entrance, dry powder outlet and a separation water out, institute
The separation aqueous solid entrance for stating drying system passes through a solid-liquid separator aqueous solid drain valve and the solid-liquid separator
Separate aqueous solid outlet connection；
One first baffle-box, the entrance of first baffle-box separates water discharging valve and the drying system by a drying system
Separation water out connection；
One first self priming pump, the entrance of first self priming pump by pipeline and solid-liquid separator separate liquid emission valve with it is described
The separation liquid outlet connection of solid-liquid separator；The outlet of first self priming pump is connected with the entrance of one first threeway；It is described
The entrance of first self priming pump is also connected by pipeline, separation water discharging valve with the separation water out of first baffle-box；
One precipitation buffering case, the precipitation buffering case has an entrance and an outlet, and the entrance of the precipitation buffering case passes through pipe
Road is connected with the first outlet in first threeway；The outlet of the precipitation buffering case is connected by precipitation buffering case blowoff valve
The entrance of one measuring pump；
One electrolysis unit, the electrolysis unit has a liquid inlet and liquid outlet, and the liquid inlet of the electrolysis unit leads to
Metering pump control valve is crossed to be connected with the outlet of the measuring pump；
One membrane cisterna, the membrane cisterna is divided into according to water flow direction scrapes slag bath, sedimentation basin, MBP ponds and clear water reserviors, it is described scrape slag bath with
The flowing of water is flowed by overflow manner between sedimentation basin, between sedimentation basin and MBP ponds；Described scrape is provided with electrolysis on slag bath
Liquid entrance, slag outlet, sewage draining exit, recoil mouth, the electrolyte entrance scraped on slag bath is by being electrolysed hydraulic control valve and the electricity
The liquid outlet connection in device is solved, the slag outlet scraped on slag bath passes through control valve and pipeline and the described second collection of slagging tap
The entrance connection of case, the sewage draining exit scraped on slag bath is by scraping slag bath blowoff valve and pipeline and second collecting box
Entrance is connected, and the mouth that recoiled on slag bath of scraping is connected by the first recoil valve and pipeline with the second outlet in first threeway
Connect；The sedimentation basin has a sewage draining exit and a recoil mouth, and the sewage draining exit of the sedimentation basin passes through sedimentation basin pollution discharge valve and pipeline
It is connected with the entrance of first self priming pump, the recoil mouthful of the sedimentation basin is connected by pipeline with first recoil valve；Institute
MBP ponds are stated with a sewage draining exit, an aeration opening, a clear water flow export and a recoil mouth, the sewage draining exit in the MBP ponds passes through MBP
Pond blowoff valve and pipeline are connected with the entrance of first self priming pump, and the aeration opening in the MBP ponds is aerated by pipeline connection one
Pump, the clear water flow export in the MBP ponds connects the entrance of one second self priming pump by MBP ponds draining valve；The clear water reserviors have
One water inlet, a cooling water recovery port and a discharge outlet, the water inlets of the clear water reserviors by clear water reserviors water intaking valve and pipeline with
The outlet connection of one the 3rd ejector, the entrance of the 3rd ejector is connected by the outlet of pipeline and second self priming pump
Connect, also there is an ozone supply mouthful on the 3rd ejector；
One ozone generator, the air intake of the ozone generator connects an air compressor machine, the ozone generator by pipeline
Ozone outlet by pipeline pick out after be divided into three branch roads, wherein first branch road passes through the first ejector ozone control valve and institute
The ozone supply mouthful connection of the first ejector is stated, Article 2 branch road passes through the second ejector ozone control valve and second jet
The ozone supply mouthful connection of device, Article 3 branch road is supplied by the ozone of the 3rd ejector ozone control valve and the 3rd ejector
Give mouth connection；The entrance of cooling circulating water pump in the ozone generator passes through cooling water control valve and pipeline and the clear water
The outlet of cooling circulating water pump in discharge outlet connection in pond, the ozone generator passes through in pipeline and the clear water reserviors
Cooling water recovery port is connected；
One elevated tank, the elevated tank has a water inlet and a delivery port, and the water inlet of the elevated tank passes through one
Booster pump, a water inlet control valve are connected with the discharge outlet of the clear water reserviors, and the delivery port of the elevated tank is picked out by pipeline
After be divided into four branch roads, wherein tie point is connected by MBR ponds recoil valve and the MBR ponds mouth that recoils, to enter to MBR ponds
Row recoil；Second branch road is connected by High Pressure Drain valve with the intelligent environment protection toilet ground flushing system, and unnecessary water is high
Pressure goes out to rinse ground, and the water after flushing is back in the vacuum sewage system again；3rd branch road passes through draining of flushing the toilet
Valve is connected with the intelligent environment protection toilet flushing system, to flush the toilet after an action of the bowels；4th branch road by first wash one's hands water control valve and
One booster pump is connected with the entrance of a pressure water tank, and the outlet of the pressure water tank is washed one's hands water control by a pressure switch, second
Valve processed and the intelligent environment protection toilet cell system of washing one's hands are connected；The sewage draining exit of the pressure water tank passes through a pressure water tank blowoff valve
It is connected with pipeline with the first self priming pump；
One control device, the control device respectively to above-mentioned vacuum sewage system, the first ejector, the first collecting box liquid
Position, the liquid level of the second collecting box, the first collecting box blowoff valve, flowmeter, the second collecting box blowoff valve, the second ejector, solid-liquid
Separator aqueous solid drain valve, the liquid level of the first baffle-box, drying system separation water discharging valve, the first self priming pump, precipitation are slow
Rush the liquid level of case, precipitation buffering case blowoff valve, measuring pump, electrolysis unit, measure pump control valve, the liquid level for scraping slag bath, sedimentation basin
Liquid level, the liquid level in MBP ponds, the liquid level of clear water reserviors, be electrolysed hydraulic control valve, control valve of slagging tap, scrape slag bath blowoff valve, first recoil
Valve, sedimentation basin pollution discharge valve, MBP ponds blowoff valve, aeration pump, MBP ponds draining valve, the second self priming pump, clear water reserviors water intaking valve, the 3rd penetrate
Flow device, ozone generator, air compressor machine, the first ejector ozone control valve, the second ejector ozone control valve, the 3rd ejector smelly
The liquid level of cooling circulating water pump, elevated tank in oxygen control valve, ozone generator, booster pump, water inlet control valve, MBR ponds are anti-
Rush valve, High Pressure Drain valve, draining valve of flushing the toilet, first wash one's hands water control valve, booster pump, the liquid level of pressure water tank, pressure switch,
Two wash one's hands water control valve, pressure water tank blowoff valve connection.
2. intelligent environment protection toilet as claimed in claim 1 is without emissions and recycles automated programming system, its feature
It is, exhaust outlet is provided with first collecting box, precipitation buffering case and membrane cisterna, and first collecting box, precipitation are slow
Rush the exhaust outlet on case and membrane cisterna to converge in a filter by pipeline, then emptied by air-introduced machine.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
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| CN201710579273.XA CN107265769A (en) | 2017-07-17 | 2017-07-17 | Intelligent environment protection toilet is without emissions and recycles automated programming system |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201710579273.XA CN107265769A (en) | 2017-07-17 | 2017-07-17 | Intelligent environment protection toilet is without emissions and recycles automated programming system |
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| CN107265769A true CN107265769A (en) | 2017-10-20 |
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| Application Number | Title | Priority Date | Filing Date |
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| CN201710579273.XA Pending CN107265769A (en) | 2017-07-17 | 2017-07-17 | Intelligent environment protection toilet is without emissions and recycles automated programming system |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
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| 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 |
| CN110080361A (en) * | 2019-06-10 | 2019-08-02 | 江苏旭云物联信息科技有限公司 | A kind of zero-emission automatically processes Porta Potti |
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| CN1657449A (en) * | 2004-02-16 | 2005-08-24 | 北京兰利东方科技有限公司 | Sewage treatment system for public lavatory |
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| CN110080361A (en) * | 2019-06-10 | 2019-08-02 | 江苏旭云物联信息科技有限公司 | A kind of zero-emission automatically processes Porta Potti |
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Application publication date: 20171020 |