CN206720971U - Interior circulating treating system for water stamp Porta Potti toilet-flushing sewage - Google Patents
Interior circulating treating system for water stamp Porta Potti toilet-flushing sewage Download PDFInfo
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- CN206720971U CN206720971U CN201720255288.6U CN201720255288U CN206720971U CN 206720971 U CN206720971 U CN 206720971U CN 201720255288 U CN201720255288 U CN 201720255288U CN 206720971 U CN206720971 U CN 206720971U
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Abstract
The interior circulating treating system for water stamp Porta Potti toilet-flushing sewage is the utility model is related to, includes three-level anaerobic organism septic tank, overflow balancing tank, hydrolysis acidification pool, aerobic biochemical pool, MBR ponds, sterilization pool, constant pressure output pump, ozone generator, MBR self priming pumps, PLC automatic control boxs；Toilet-flushing sewage is successively by three-level anaerobic organism septic tank is handled, hydrolysis acidification pool is handled, aerobic biochemical pool is handled, MBR ponds are handled, after sterilization pool processing, the toilet flushing device recycling that toilet flushing is supplied to Porta Potti is exported through clear water in constant pressure output pump extraction sterilization pool.The interior circulating disposal process and system of toilet-flushing sewage provided by the utility model, by the synergy of high-performance bio processing unit and disinfection unit, toilet-flushing sewage is thoroughly purified and be converted into clean water, realize toilet-flushing sewage watershed management and recycling.Continuous, complete systematization and recycling treatment are realized using the water stamp bio-toilet of the internal circulation system.
Description
Technical field
Porta Potti toilet-flushing sewage processing technology field is the utility model is related to, is specifically related to be used for water stamp movement lavatory
The interior circulating disposal process of institute's toilet-flushing sewage, the interior circulating treating system of the toilet-flushing sewage is further related to.
Background technology
Bio-toilet refer to have environment is not polluted, various resources can be made full use of, emphasize pollutant purification and
A kind of lavatory of resource circulation utilization concept and function.How by the toilet-flushing sewage of traditional water stamp Porta Potti
Recycled after reason, then contribute to such Porta Potti making the bio-toilet with environmental protection, power saving function, very have and promote
Value.
Utility model content
Technical problem to be solved in the utility model is to provide a kind of for the interior of water stamp Porta Potti toilet-flushing sewage
Circulating treating system, for realizing the purified treatment of water stamp Porta Potti toilet-flushing sewage and interior recycling.
In order to solve the above technical problems, the utility model provides following technical scheme：Flushed the toilet for water stamp Porta Potti
The interior circulating treating system of sewage, include three-level anaerobic organism septic tank, overflow balancing tank, hydrolysis acidification pool, aerobic biochemical
Pond, MBR ponds, sterilization pool, constant pressure output pump, ozone generator, MBR self priming pumps, PLC automatic control boxs；
The three-level anaerobic organism septic tank is provided with by being communicated in overflow balancing tank communicating pipe in the overflow balancing tank
Elevator pump and the first liquid level sensor, the lifting pump output terminal are communicated in hydrolysis acidification pool, and the hydrolysis acidification pool is under
The flowing hole in portion is communicated in aerobic biochemical pool, and the aerobic biochemical pool is communicated in MBR ponds, the MBR by the spout hole on top
MBR membrane separation plants are provided with pond, the MBR self priming pumps input is communicated in MBR ponds, output end is communicated in sterilization pool, described
Ultraviolet disinfection lamp is fixed with sterilization pool, the ozone generator is communicated in sterilization pool, and the constant pressure output pump input connects
Pass through sterilization pool；The second liquid level sensor, first liquid level sensor, the second liquid level sensor are fixed with the MBR ponds
It is electrically connected in PLC automatic control box inputs, the elevator pump, MBR self priming pumps, ozone generator, constant pressure output pump point
PLC automatic control box output ends are not electrically connected to；
The three-level anaerobic organism septic tank, hydrolysis acidification pool, aerobic biochemical pool, MBR are inoculated with seed sludge in pond
And monitoring temperature regulating system is respectively and fixedly provided with, the solution acidification pool, aerobic biochemical pool, oxygen content monitoring is respectively and fixedly provided with MBR ponds
Regulating system.
On the basis of such scheme, the monitoring temperature regulating system include for detect water temperature temperature sensor,
Heated at constant temperature pipe, electrically heated boiler, the three-level anaerobic organism septic tank, hydrolysis acidification pool, aerobic biochemical pool, in MBR ponds
Temperature sensor and heated at constant temperature pipe are fixed with, the heated at constant temperature pipe is communicated in electrically heated boiler, the temperature sensor electricity
PLC automatic control box inputs are connected to, the electrically heated boiler is electrically connected to PLC automatic control box output ends；The oxygen contains
Amount monitoring regulating system includes being used for the oxygen level sensor, rubber micro-hole aerator, revolution blower fan for detecting water oxygen level, institute
State hydrolysis acidification pool, aerobic biochemical pool, be respectively and fixedly provided with oxygen level sensor and rubber micro-hole aerator, the rubber in MBR ponds
Micro-hole aerator is communicated in revolution blower fan, and the oxygen level sensor is electrically connected to PLC automatic control box inputs, the revolution
Blower fan is electrically connected to PLC automatic control box output ends.
On the basis of such scheme, the three-level anaerobic organism septic tank includes the first pond being sequentially distributed side by side,
Two ponds and the 3rd pond, between first pond and the second pond, pass through downflow weir and downflow weir phase between the second pond and the 3rd pond
Logical flow tube connection；3rd pond is by being communicated in overflow balancing tank communicating pipe.
On the basis of such scheme, also include that an input is communicated in sterilization pool, output end is communicated in MBR UF membranes
The MBR backwashing pumps of equipment, the MBR backwashing pumps are electrically connected to PLC automatic control box output ends.
On the basis of such scheme, also include a thermal evaporation system being communicated in sterilization pool, consolidate in the sterilization pool
Surely there is the 3rd liquid level sensor；3rd liquid level sensor is electrically connected to PLC automatic control box inputs, the thermal evaporation system
System is electrically connected to PLC automatic control box output ends.
On the basis of such scheme, also include that an input is connected to ozone generator, output end is connected to outside constant pressure
The ozone mixing pump of defeated pump input；The ozone mixing pump is electrically connected to PLC automatic control box output ends.
On the basis of such scheme, also include that an input is connected to MBR membrane separation plants, output end is connected to hydrolysis
Sludge reflux pump in acidification pool, the sludge reflux pump are electrically connected to PLC automatic control box output ends
The utility model has an advantageous effect in that compared with prior art：Toilet-flushing sewage provided by the utility model it is interior
Circulating treating system, by the synergy of high-performance bio processing unit and disinfection unit, enable toilet-flushing sewage thoroughly net
Change is converted into clean water, and water quality reaches China's Treated sewage reusing relevant criterion and requires (GB/T18920), fundamentally realizes and flush the toilet
Sewage watershed management and recycling.Realized over time and space continuously using the water stamp bio-toilet of the internal circulation system
, complete systematization and recycling treatment, breach dependence of traditional water closet to clean water, meet ecological environment
The requirement of sustainable development, meanwhile, full-automatic operation and management mode avoids manual contact, completely eliminates intersection sense
Dye, very with promotional value.
Brief description of the drawings
Fig. 1 is Tthe utility model system structural representation；
Fig. 2 is the structural representation of the utility model three-level anaerobic organism septic tank.
In figure marked as：1- toilet flushing devices, 2- three-level anaerobic organism septic tanks, the ponds of 21- first, the ponds of 22- second,
The ponds of 23- the 3rd, 24- downflow weirs, 25- flow tubes, 26- temperature sensors, 27- heated at constant temperature pipes, 28- electrically heated boilers, 3- overflow
Stream balancing tank, 31- elevator pumps, 32- communicating pipes, the liquid level sensors of 33- first, 4- hydrolysis acidification pools, 41- flowing holes, 5- are aerobic
Biochemistry pool, 51- spout holes, 52- oxygen level sensors, 53- rubber micro-hole aerators, 54- revolution blower fans, 6-MBR ponds, 61-MBR
Membrane separation plant, 62-MBR self priming pumps, 63-MBR backwashing pumps, 64- sludge reflux pumps, the liquid level sensors of 65- second, 7- sterilizations
Pond, 71- ultraviolet disinfection lamps, 72- ozone generators, 73- thermal evaporation systems, the liquid level sensors of 74- the 3rd are defeated outside 8- constant pressures
Pump, 81- ozone mixing pumps, 9-PLC automatic control boxs.
Embodiment
In order that the purpose of this utility model, technical scheme and advantage are more clearly understood, below in conjunction with accompanying drawing and implementation
Example, the utility model is further elaborated.It should be appreciated that specific embodiment described herein is only explaining
The utility model, it is not used to limit the utility model.
Understand referring to Figures 1 and 2, the utility model provides a kind of interior circulation for water stamp Porta Potti toilet-flushing sewage
Processing system, the system include three-level anaerobic organism septic tank 2, overflow balancing tank 3, hydrolysis acidification pool 4, aerobic biochemical pool 5,
MBR ponds 6, sterilization pool 7, constant pressure output pump 8, ozone generator 72, MBR self priming pumps 62, PLC automatic control boxs 9.In three-level anaerobism
Seed sludge in biological septic tank 2 is the granule sludge of industrial UASB reactors, and be have passed through before inoculation at activation elutriation
Reason.Using polyvinyl chloride composition filler as bio-carrier in hydrolysis acidification pool 4, aerobic biochemical pool 5, MBR ponds 6, with city
The second pond returned sludge of sewage treatment plant is as seed sludge, and is filtered large granular impurity in activated sludge before inoculation
Remove.
The three-level anaerobic organism septic tank 2 is by being communicated in overflow balancing tank 3, the overflow balancing tank 3 communicating pipe 32
Interior to be provided with the liquid level sensor 33 of elevator pump 31 and first, the output end of elevator pump 31 is communicated in hydrolysis acidification pool 4, the hydrolysis
Acidification pool 4 is communicated in aerobic biochemical pool 5, the spout hole 51 that the aerobic biochemical pool 5 passes through top by the flowing hole 41 of bottom
MBR ponds 6 are communicated in, are provided with MBR membrane separation plants 61 in the MBR ponds 6, the input of MBR self priming pumps 62 is communicated in MBR ponds
6th, output end is communicated in sterilization pool 7, and the ozone generator 72 is communicated in sterilization pool 7, the input of constant pressure output pump 8 connection
In being fixed with ultraviolet disinfection lamp 71 in sterilization pool 7, the sterilization pool 7.The second liquid level sensor is fixed with the MBR ponds 6
65, first liquid level sensor 33, the second liquid level sensor 65 are electrically connected in the input of PLC automatic control boxs 9, institute
State elevator pump 31, MBR self priming pumps 62, ozone generator 72, constant pressure output pump 8 and be electrically connected and exported in PLC automatic control boxs 9
End.
Therein, the three-level anaerobic organism septic tank 2 includes the first pond 21 being sequentially distributed side by side, the and of the second pond 22
3rd pond 23, between the pond 22 of the first pond 21 and second, between the second pond 22 and the 3rd pond 23 by downflow weir 24, with overflowing
The flow tube 25 that stream weir 24 communicates connects；3rd pond 23 is communicated in overflow balancing tank 3 by communicating pipe 32.Toilet-flushing sewage is certainly
The toilet flushing device 1 of Porta Potti is flowed into the first pond 21 of three-level anaerobic organism septic tank 2, through the second pond 22, the 3rd pond
23 flow into overflow balancing tank 3, when the first liquid level sensor 33 detects that water level reaches predetermined value in overflow balancing tank 3, PLC
Automatic control box 9 then manipulates elevator pump 31 and worked in sewage lifting input hydrolysis acidification pool 4.Sewage by hydrolysis acidification pool 4,
Aerobic biochemical pool 5 enters in MBR ponds 6, when the second liquid level sensor 65 detects that water level is higher than predetermined value in MBR ponds 6, PLC
Automatic control box 9 then manipulates MBR self priming pumps 62 and worked, and clear water in MBR ponds 6 is extracted in the lower sterilization pool 7 of input.Clear water is sterilizing
In pond 7 after ozone and ultraviolet ray sterilization bactericidal decolorization, the lavatory that supply Porta Potti is extracted by constant pressure output pump 8 is rushed
Water installations 1 recycle.
The three-level anaerobic organism septic tank 2, hydrolysis acidification pool 4, aerobic biochemical pool 5, it is inoculated with being inoculated with MBR ponds 6
Sludge and monitoring temperature regulating system is respectively and fixedly provided with, the hydrolysis acidification pool 4, aerobic biochemical pool 5, is respectively and fixedly provided with oxygen in MBR ponds 6
Content monitors regulating system.It is therein, the monitoring temperature regulating system include for detect water temperature temperature sensor 26,
Heated at constant temperature pipe 27, electrically heated boiler 28, the three-level anaerobic organism septic tank 2, hydrolysis acidification pool 4, aerobic biochemical pool 5, MBR
Temperature sensor 26 and heated at constant temperature pipe 27 are respectively and fixedly provided with pond 6, the heated at constant temperature pipe 27 is communicated in electrically heated boiler 28, institute
State temperature sensor 26 and be electrically connected to the input of PLC automatic control boxs 9, the electrically heated boiler 28 is electrically connected to PLC and controlled automatically
The output end of case 9 processed, temperature in each pond is controlled to maintain in the range of certain constant temperature using monitoring temperature regulating system.It is therein, institute
State oxygen content monitoring regulating system include being used for detecting the oxygen level sensor 52 of water oxygen level, rubber micro-hole aerator 53,
Turn round blower fan 54, the hydrolysis acidification pool 4, aerobic biochemical pool 5, be respectively and fixedly provided with oxygen level sensor 52 in MBR ponds 6 and rubber is micro-
Hole aerator 53, the rubber micro-hole aerator 53 are communicated in revolution blower fan 54, and the oxygen level sensor 52 is electrically connected to PLC
The input of automatic control box 9, the revolution blower fan 54 are electrically connected to the output end of PLC automatic control boxs 9；Monitored and adjusted using oxygen content
Section system controls oxygen content in a constant range.
Preferably, the system also includes that an input is communicated in sterilization pool 7, output end is communicated in MBR UF membranes and set
Standby 61 MBR backwashing pumps 63, the MBR backwashing pumps 63 are electrically connected in the output end of PLC automatic control boxs 9.With MBR backwashing pumps
63 clear water extracted in sterilization pool 7 carry out backwash processing to the MBR membrane separation plants 61 in MBR ponds 6；Moreover, MBR self priming pumps 62
Work 10min then carries out a backwash MBR membrane separation plants 1min of MBR backwashing pumps 63.Contain when MBR membrane separation plants 61 are immersed in
When having in the sewage of sludge, because sludge content is controlled in 4000mg/l or so, so MBR membrane separation plants 61 easily block,
It can effectively prevent MBR membrane separation plants 61 from blocking by using air agitation effect and the backwash of MBR backwashing pumps 63 effect.Together
When, then provided with an input be connected to MBR membrane separation plants 61, output end is connected to sludge reflux pump in hydrolysis acidification pool 7
64, the sludge reflux pump 64 is electrically connected to the output end of PLC automatic control boxs 9, realizes sewage again using sludge reflux pump 64
Processing.
Preferably, the system also includes a thermal evaporation system 73 being communicated in sterilization pool 7, the thermal evaporation system 73
The output end of PLC automatic control boxs 9 is electrically connected to, the 3rd liquid level sensor 74 is fixed with the sterilization pool 7, the 3rd liquid level passes
Sensor 74 is electrically connected to the input of PLC automatic control boxs 9.When the 3rd liquid level sensor 74 detects that clear water is higher than in sterilization pool 7
During predetermined value, the automatic start thermal evaporation system 73 of PLC automatic control boxs 9 work evaporation clear water is maintained at clear water in sterilization pool 7
In predetermined range, to ensure the water balance in the whole circulatory system.
Preferably, the system also include an input be connected to ozone generator 7, output end be connected to it is defeated outside constant pressure
The ozone mixing pump 81 of the input of pump 8, the ozone mixing pump 81 are electrically connected to the output end of PLC automatic control boxs 9, utilize ozone
Generator 72 and ozone mixing pump 81 ozone mixed in clear water, then extract supply Porta Potti by constant pressure output pump 8
Toilet flushing device 1 recycles, and can play disinfection effect.
Interior the circulating disposal process implementation process and operation principle of said system be：
Toilet-flushing sewage is successively by three-level anaerobic organism septic tank 2 is handled, hydrolysis acidification pool 4 is handled, at aerobic biochemical pool 5
Reason, MBR ponds 6 are handled, after the processing of sterilization pool 7, and extracting clear water in sterilization pool 7 through constant pressure output pump 8 exports to Porta Potti for rushing
The toilet flushing device 1 for washing lavatory recycles.Seed sludge in three-level anaerobic organism septic tank 2 is industrial UASB reactors
Granule sludge, and have passed through before inoculation activation elutriation processing.Adopted in hydrolysis acidification pool 4, aerobic biochemical pool 5, MBR ponds 6
By the use of polyvinyl chloride composition filler as bio-carrier, using the second pond returned sludge of municipal sewage plant to be dirty as inoculation
Mud, and filter out large granular impurity in activated sludge before inoculation.
(1) in the processing procedure of three-level anaerobic organism septic tank 2, temperature in three-level anaerobic organism septic tank 2 is kept to be in
In the range of 23 DEG C -27 DEG C, toilet-flushing sewage stops 12-24 hours in three-level anaerobic organism septic tank 2, makes toilet-flushing sewage and the pond
Interior seed sludge is sufficiently mixed contact.Therein, toilet-flushing sewage stops 12-24 hours in three-level anaerobic organism septic tank 2,
Dwell time of sewage is extended, sedimentation effect and effluent quality can be improved.
Specifically：The three-level anaerobic organism septic tank 2 includes the first pond 21 being sequentially distributed side by side, the second pond 22 and
Three ponds 23, pass through downflow weir 24 and overflow between the pond 22 of the first pond 21 and second, between the second pond 22 and the 3rd pond 23
The flow tube 25 that weir 24 communicates connects；Toilet-flushing sewage enters in the first pond 21, and the particulate matter contained in its sewage is made in gravity
It is upper with lower precipitation, sewage, separation of solid and liquid is realized, sewage enters in the second pond 22 from downflow weir 24, flow tube 25；Then from
Two ponds, 22 bottom up motion, under turbulent water effect, the seed sludge in the second pond 22 is in suspended state and mixed with sewage
Splice grafting touches, and carries out anaerobic fermentation；Then the sewage in the second pond 22 enters in the 3rd pond 23 from downflow weir 24, flow tube 25, from
3rd pond, 23 bottom up motion, under turbulent water effect, the seed sludge in the 3rd pond 23 is in suspended state and sewage
Mixing contact, carries out anaerobic fermentation.
The three-level anaerobic organism septic tank 2 plays settlement of sewage and anaerobism hair equivalent to the combination of anaerobic pond and sedimentation basin
Sedimentation basin is played a part of in the effect of ferment, the first pond 21, and fermentation is played a part of in the second pond 22 and the 3rd pond 23, so as to reach one
The multi-purpose purpose in pond, the organic matter of the suspension and can degraded sewage in fecal sewage can be removed.
Then the toilet-flushing sewage after the processing of three-level anaerobic organism septic tank 2 enters in overflow balancing tank 3, utilizes elevator pump
31 are lifted into hydrolysis acidification pool 4.Therein, overflow balancing tank 3 is the effect for reconciling front and rear water inlet, to three-level anaerobic organismization
Toilet-flushing sewage after the processing of manure pit 2 has the function of a storage, plays a cushioning effect to elevator pump 31 below, prevents from being lifted
The frequent starting of pump 31 and damage elevator pump.It can be used in sensed water level provided with the first liquid level sensor in overflow balancing tank 3 and lead to
The water level height crossed in the control balancing tank 3 of PLC automatic control boxs 9, start elevator pump 31 when water level is high into hydrolysis acidification pool 4
Water lift, stop elevator pump 31 during low water level and work.
(2) in the processing procedure of hydrolysis acidification pool 4, air is filled with for hydrolysis acidification pool 4, pond is included oxygen content control and exists
Below 2mg/l, using the perturbation action of air, in pond, seed sludge is sufficiently mixed with sewage contacts, by particulate matter in sewage
Retain and adsorb with colloidal substance, by macromolecular, be difficult to after degradable chemical is converted into the small-molecule substance being readily biodegradable,
It is re-released into liquid；Then sewage enters from the flowing hole below hydrolysis acidification pool carries out next step in aerobic biochemical pool
Fine processing.
(3) in the processing procedure of aerobic biochemical pool 5, under the disturbance being largely aerated, the control of sewage oxygen content is made in 2-
5mg/l, degraded using its seed sludge or adsorb carbon containing, ammonia nitrogen, phosphorus organic pollution materials in water, such as most COD, BOD, ammonia
Nitrogen etc. is all consumed in aerobic biochemical pool 5 by bacterium, is converted into innocuous substance；Then sewage is from aerobic biochemical pool top
Spout hole enters in MBR ponds.
(4) in the processing procedure of MBR ponds 6, air is filled with for MBR ponds 6, is acted on using air agitation, seed sludge in pond
It is sufficiently mixed and contacts with sewage, further removes harmful substance.Activated sludge and macromolecular are had using MBR membrane separation plants 61
Machine thing is retained, and more than 95% harmful substance and 99% suspension have been removed by the sewage of MBR membrane separation plants 61
And bacterium.The second liquid level sensor detection MBR pool inner waters position situation is set in MBR ponds 6, when liquid level is higher than predetermined value in MBR ponds 6
When, the clear water in the extraction MBR of MBR self priming pumps 62 ponds 6 is started by PLC automatic control boxs 9 and inserted in sterilization pool 7, to maintain MBR
Water level trend balances in pond 6.
MBR backwashing pumps 63 are also associated between MBR ponds 6 and sterilization pool 7, are extracted using MBR backwashing pumps 63 in sterilization pool 7
Clear water in MBR ponds 6 MBR membrane separation plants 61 carry out backwash processing；Moreover, MBR self priming pumps 62 work, 10min is then carried out
Backwash MBR membrane separation plants 1min of MBR backwashing pumps 63.When MBR membrane separation plants 61 are immersed in the sewage containing sludge
When, because sludge content is controlled in 4000mg/l or so, so MBR membrane separation plants 61 easily block, disturbed by using air
Action use and MBR backwashing pumps 63 backwash act on can effectively prevent MBR membrane separation plants 61 from blocking.It is meanwhile then defeated provided with one
Enter that end is connected to MBR membrane separation plants 61, output end is connected to sludge reflux pump 64 in hydrolysis acidification pool 4, utilize sludge to return
Stream pump 64 realizes the reprocessing of sewage.
(5) in the processing procedure of sterilization pool 7, carry out sterilization for input ozone in sterilization pool 7 using ozone generator 72 and disappear
Poison, meanwhile, coordinate in sterilization pool 7 and carry out carrying out ultraviolet sterilization processing, reach the sterilization to clear water and decolorization effect；
Clear water after sterilized pond 7 is handled then extracts supply Porta Potti for toilet flushing use by constant pressure output pump 8.By sterilization
Clear water after the processing of pond 7 carries out ozone mixed processing before constant pressure output pump 8 is conveyed to Porta Potti recycling to the clear water.
Meanwhile a set of thermal evaporation system 73 for being used to evaporate clear water is configured for sterilization pool 7, utilize the 3rd liquid level sensor in sterilization pool
Water level in sterilization pool is detected, when clear water is higher than predetermined value in sterilization pool 7, starting the work evaporation clear water of thermal evaporation system 73 makes
Clear water is maintained in predetermined range in sterilization pool 7, to ensure the water balance in the whole circulatory system.
Claims (7)
1. the interior circulating treating system for water stamp Porta Potti toilet-flushing sewage, it is characterised in that：Include the life of three-level anaerobism
Materialization manure pit, overflow balancing tank, hydrolysis acidification pool, aerobic biochemical pool, MBR ponds, sterilization pool, constant pressure output pump, ozone generator,
MBR self priming pumps, PLC automatic control boxs；
The three-level anaerobic organism septic tank is provided with lifting by being communicated in overflow balancing tank communicating pipe in the overflow balancing tank
Pump and the first liquid level sensor, the lifting pump output terminal are communicated in hydrolysis acidification pool, and the hydrolysis acidification pool passes through bottom
Flowing hole is communicated in aerobic biochemical pool, and the aerobic biochemical pool is communicated in MBR ponds by the spout hole on top, in the MBR ponds
Provided with MBR membrane separation plants, the MBR self priming pumps input is communicated in MBR ponds, output end is communicated in sterilization pool, the sterilization
Ultraviolet disinfection lamp is fixed with pond, the ozone generator is communicated in sterilization pool, and the constant pressure output pump input is communicated in
Sterilization pool；The second liquid level sensor, first liquid level sensor, the second liquid level sensor difference are fixed with the MBR ponds
PLC automatic control box inputs are electrically connected to, the elevator pump, MBR self priming pumps, ozone generator, constant pressure output pump are electric respectively
It is connected to PLC automatic control box output ends；
The three-level anaerobic organism septic tank, hydrolysis acidification pool, aerobic biochemical pool, seed sludge and is inoculated with MBR ponds
It is fixed with monitoring temperature regulating system, the solution acidification pool, aerobic biochemical pool, is respectively and fixedly provided with oxygen content monitoring regulation in MBR ponds
System.
2. the interior circulating treating system according to claim 1 for water stamp Porta Potti toilet-flushing sewage, its feature exists
In：The monitoring temperature regulating system includes the temperature sensor, heated at constant temperature pipe, electrically heated boiler for detecting water temperature,
The three-level anaerobic organism septic tank, hydrolysis acidification pool, aerobic biochemical pool, MBR are respectively and fixedly provided with temperature sensor and constant temperature in pond
Heating tube, the heated at constant temperature pipe are communicated in electrically heated boiler, and the temperature sensor is electrically connected to the input of PLC automatic control boxs
End, the electrically heated boiler are electrically connected to PLC automatic control box output ends；The oxygen content monitoring regulating system includes being used to examine
Survey the oxygen level sensor of water oxygen level, rubber micro-hole aerator, revolution blower fan, the hydrolysis acidification pool, aerobic biochemical pool,
Oxygen level sensor and rubber micro-hole aerator are respectively and fixedly provided with MBR ponds, the rubber micro-hole aerator is communicated in revolution blower fan,
The oxygen level sensor is electrically connected to PLC automatic control box inputs, and the revolution blower fan is electrically connected to PLC automatic control boxs
Output end.
3. the interior circulating treating system according to claim 1 for water stamp Porta Potti toilet-flushing sewage, its feature exists
In：The three-level anaerobic organism septic tank includes the first pond being sequentially distributed side by side, the second pond and the 3rd pond, first pond
Connected between the second pond, between the second pond and the 3rd pond by downflow weir, the flow tube communicated with downflow weir；Described 3rd
Pond is by being communicated in overflow balancing tank communicating pipe.
4. the interior circulating treating system according to claim 1 for water stamp Porta Potti toilet-flushing sewage, its feature exists
In：Also include an input and be communicated in the MBR backwashing pumps that sterilization pool is interior, output end is communicated in MBR membrane separation plants, it is described
MBR backwashing pumps are electrically connected to PLC automatic control box output ends.
5. the interior circulating treating system according to claim 1 for water stamp Porta Potti toilet-flushing sewage, its feature exists
In：Also include a thermal evaporation system being communicated in sterilization pool, the 3rd liquid level sensor is fixed with the sterilization pool；It is described
3rd liquid level sensor is electrically connected to PLC automatic control box inputs, and the thermal evaporation system is electrically connected to PLC automatic control boxs
Output end.
6. the interior circulating treating system according to claim 1 for water stamp Porta Potti toilet-flushing sewage, its feature exists
In：Also include that an input is connected to ozone generator, output end is connected to the ozone mixing pump of constant pressure output pump input；
The ozone mixing pump is electrically connected to PLC automatic control box output ends.
7. the interior circulating treating system according to claim 1 for water stamp Porta Potti toilet-flushing sewage, its feature exists
In：Also include that an input is connected to MBR membrane separation plants, output end is connected to sludge reflux pump in hydrolysis acidification pool,
The sludge reflux pump is electrically connected to PLC automatic control box output ends.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720255288.6U CN206720971U (en) | 2017-03-07 | 2017-03-07 | Interior circulating treating system for water stamp Porta Potti toilet-flushing sewage |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720255288.6U CN206720971U (en) | 2017-03-07 | 2017-03-07 | Interior circulating treating system for water stamp Porta Potti toilet-flushing sewage |
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| Publication Number | Publication Date |
|---|---|
| CN206720971U true CN206720971U (en) | 2017-12-08 |
Family
ID=60502032
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201720255288.6U Expired - Fee Related CN206720971U (en) | 2017-03-07 | 2017-03-07 | Interior circulating treating system for water stamp Porta Potti toilet-flushing sewage |
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Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106698863A (en) * | 2017-03-07 | 2017-05-24 | 哈尔滨盛龙华环保科技发展有限公司 | Inner circulation treatment process and system for water flushing type moving toilet flushing sewage |
| CN108640442A (en) * | 2018-07-12 | 2018-10-12 | 成都中恒逸安环保科技有限公司 | The cycling use of water night soil-treatment lavatory of intelligence control |
| CN111333190A (en) * | 2020-04-08 | 2020-06-26 | 苏州道藤环保科技有限公司 | Batch water inlet continuous water outlet sewage treatment device and treatment method |
| CN113501623A (en) * | 2021-07-27 | 2021-10-15 | 浙江新睿环保科技有限公司 | Public toilet sewage online recycling system |
-
2017
- 2017-03-07 CN CN201720255288.6U patent/CN206720971U/en not_active Expired - Fee Related
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106698863A (en) * | 2017-03-07 | 2017-05-24 | 哈尔滨盛龙华环保科技发展有限公司 | Inner circulation treatment process and system for water flushing type moving toilet flushing sewage |
| CN108640442A (en) * | 2018-07-12 | 2018-10-12 | 成都中恒逸安环保科技有限公司 | The cycling use of water night soil-treatment lavatory of intelligence control |
| CN111333190A (en) * | 2020-04-08 | 2020-06-26 | 苏州道藤环保科技有限公司 | Batch water inlet continuous water outlet sewage treatment device and treatment method |
| CN113501623A (en) * | 2021-07-27 | 2021-10-15 | 浙江新睿环保科技有限公司 | Public toilet sewage online recycling system |
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