CN107915374A - Solar energy type cold district sanitary sewage disposal integration apparatus and its processing method - Google Patents
Solar energy type cold district sanitary sewage disposal integration apparatus and its processing method Download PDFInfo
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- CN107915374A CN107915374A CN201711184608.4A CN201711184608A CN107915374A CN 107915374 A CN107915374 A CN 107915374A CN 201711184608 A CN201711184608 A CN 201711184608A CN 107915374 A CN107915374 A CN 107915374A
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- 239000010865 sewage Substances 0.000 title claims abstract description 54
- 230000010354 integration Effects 0.000 title claims abstract description 20
- 238000003672 processing method Methods 0.000 title description 3
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 40
- 230000001105 regulatory effect Effects 0.000 claims abstract description 30
- 239000010802 sludge Substances 0.000 claims abstract description 19
- 238000012545 processing Methods 0.000 claims abstract description 15
- 238000000926 separation method Methods 0.000 claims abstract description 11
- 238000000034 method Methods 0.000 claims abstract description 9
- 230000009977 dual effect Effects 0.000 claims abstract description 4
- 230000037452 priming Effects 0.000 claims description 17
- 238000010992 reflux Methods 0.000 claims description 15
- 238000007654 immersion Methods 0.000 claims description 12
- 239000012510 hollow fiber Substances 0.000 claims description 9
- 238000005273 aeration Methods 0.000 claims description 7
- 230000008676 import Effects 0.000 claims description 6
- 239000007788 liquid Substances 0.000 claims description 6
- 238000007667 floating Methods 0.000 claims description 5
- 244000005700 microbiome Species 0.000 claims description 4
- 238000000605 extraction Methods 0.000 claims description 3
- 230000005484 gravity Effects 0.000 claims description 3
- 238000010438 heat treatment Methods 0.000 claims description 3
- 238000012423 maintenance Methods 0.000 claims description 3
- 239000003403 water pollutant Substances 0.000 claims description 3
- 238000012258 culturing Methods 0.000 claims description 2
- 238000012216 screening Methods 0.000 claims description 2
- 241000894006 Bacteria Species 0.000 claims 1
- 230000000694 effects Effects 0.000 abstract description 6
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 4
- 229910052760 oxygen Inorganic materials 0.000 description 4
- 239000001301 oxygen Substances 0.000 description 4
- 238000010276 construction Methods 0.000 description 3
- 239000002351 wastewater Substances 0.000 description 3
- 239000007900 aqueous suspension Substances 0.000 description 2
- 230000008901 benefit Effects 0.000 description 2
- 238000011161 development Methods 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 230000008569 process Effects 0.000 description 2
- 238000004065 wastewater treatment Methods 0.000 description 2
- 238000013019 agitation Methods 0.000 description 1
- 230000015556 catabolic process Effects 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 239000000306 component Substances 0.000 description 1
- 239000008358 core component Substances 0.000 description 1
- 238000006731 degradation reaction Methods 0.000 description 1
- 238000013461 design Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 230000005611 electricity Effects 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 239000003344 environmental pollutant Substances 0.000 description 1
- 239000000835 fiber Substances 0.000 description 1
- 230000006872 improvement Effects 0.000 description 1
- 239000012528 membrane Substances 0.000 description 1
- 230000007269 microbial metabolism Effects 0.000 description 1
- 239000005416 organic matter Substances 0.000 description 1
- 244000052769 pathogen Species 0.000 description 1
- 230000001717 pathogenic effect Effects 0.000 description 1
- 231100000719 pollutant Toxicity 0.000 description 1
- 239000011148 porous material Substances 0.000 description 1
- 230000009467 reduction Effects 0.000 description 1
- 230000003014 reinforcing effect Effects 0.000 description 1
- 230000000630 rising effect Effects 0.000 description 1
- 230000035939 shock Effects 0.000 description 1
- 238000001179 sorption measurement Methods 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
- 230000002277 temperature effect Effects 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F9/00—Multistage treatment of water, waste water or sewage
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/001—Processes for the treatment of water whereby the filtration technique is of importance
-
- 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
- C02F1/30—Treatment of water, waste water, or sewage by irradiation
- C02F1/32—Treatment of water, waste water, or sewage by irradiation with ultraviolet light
- C02F1/325—Irradiation devices or lamp constructions
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2201/00—Apparatus for treatment of water, waste water or sewage
- C02F2201/002—Construction details of the apparatus
- C02F2201/007—Modular design
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2201/00—Apparatus for treatment of water, waste water or sewage
- C02F2201/009—Apparatus with independent power supply, e.g. solar cells, windpower or fuel cells
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2301/00—General aspects of water treatment
- C02F2301/04—Flow arrangements
-
- 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
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F3/00—Biological treatment of water, waste water, or sewage
- C02F3/02—Aerobic processes
- C02F3/08—Aerobic processes using moving contact bodies
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F3/00—Biological treatment of water, waste water, or sewage
- C02F3/02—Aerobic processes
- C02F3/12—Activated sludge processes
- C02F3/1236—Particular type of activated sludge installations
- C02F3/1268—Membrane bioreactor systems
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F3/00—Biological treatment of water, waste water, or sewage
- C02F3/30—Aerobic and anaerobic processes
- C02F3/302—Nitrification and denitrification treatment
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F3/00—Biological treatment of water, waste water, or sewage
- C02F3/34—Biological treatment of water, waste water, or sewage characterised by the microorganisms used
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
- Y02A20/00—Water conservation; Efficient water supply; Efficient water use
- Y02A20/20—Controlling water pollution; Waste water treatment
- Y02A20/208—Off-grid powered water treatment
- Y02A20/212—Solar-powered wastewater sewage treatment, e.g. spray evaporation
Landscapes
- Life Sciences & Earth Sciences (AREA)
- Hydrology & Water Resources (AREA)
- Engineering & Computer Science (AREA)
- Environmental & Geological Engineering (AREA)
- Water Supply & Treatment (AREA)
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Physical Water Treatments (AREA)
- Heat Treatment Of Water, Waste Water Or Sewage (AREA)
Abstract
The present invention relates to a kind of solar energy type cold district sanitary sewage disposal integration apparatus and its method, including grid pond, regulating reservoir, bioselection pond, anoxic pond, aerobic tank, MBR ponds, ultraviolet sterilizer, equipment room.Sanitary sewage enters grid pond, it is promoted to again by the first elevator pump in regulating reservoir, sewage is promoted to bioselection pond by the second elevator pump pump, anoxic pond is flowed into again, aerobic tank is promoted to by the 3rd elevator pump again, at the same the mixed liquor in aerobic tank, MBR ponds can single-pipeline or dual circuit be back in anoxic pond and carry out denitrogenation processing, further optimizing water quality, finally enter in MBR ponds and carry out mud-water separation by plate film assembly, water outlet is by MBR self-priming pumpeds.Can solve the problems, such as remote districts, effective processing of power shortage area countryside sanitary sewage and other processing equipment winter low temperature systems can not normal operation or sewage treating efficiency it is low, the problems such as effectively solving poor mud-water separation poor performance, denitrification effect under low temperature, sludge bulking.
Description
Technical field
The invention belongs to environmental technology field wastewater treatment direction, supported more particularly to the sanitary sewage to rural area and herding
The processing of sewage is grown, is specially a kind of solar energy type cold district sanitary sewage disposal integration apparatus and its processing method.
Background technology
Rural domestic sewage treatment itself the characteristics of determine the processing that be different from general municipal sewage, country sewage
General flow is small, daily variation factor is big, pollutant component is complicated, away from blowdown pipe network and big water body.Rural domestic sewage treatment
It is also responsible for the features such as right disunity, management mode are single, public participation dynamics is inadequate, supervisory engineering staff lack.Tradition
Construction of wastewater treatment plant pattern be not suitable with the construction of rural domestic sewage treatment engineering.Compared to traditional cities sewage treatment plant
Construction mode, integrated equipment for sewage treatment technological process is simple, take up an area less, operational management is simple, with traditional large-scale dirt
Water treatment system is compared, and has irreplaceable advantage and more vast potential for future development in rural area.
Cold district sewage disposal device is generally influenced be subject to cryogenic conditions, and microbial metabolism is slow during winter operation,
Organic matter degradation inefficient, the settling property of activated sludge are gradually lowered with the reduction of temperature, go out water suspension content height.It is anxious
Need to ensure the good sewage disposal device of certain treatment effeciency, mud-water separation under a kind of low temperature.The sewage disposal of existing cold district
The characteristics of facility is：
（1）The impact load of resistance to waterpower energy force difference, processing water scope is small, and effluent quality is unstable；
（2）Sewage treating efficiency is poor under low temperature, and especially denitrogenation processing is obvious by low temperature effect；
（3）The mud-water separation poor performance of secondary settling tank, goes out water suspension content height under low temperature；
（4）To ensure treatment effeciency certain at low temperature, equipment needs extra electric power energy heated waste water；
（5）Original microorganism is not fully used in sanitary sewage；
（6）If high organic content in waste water, sludge bulking problem easily occurs.
Currently, sewage drainage standard gradually steps up, and existing equipment can not meet people's living needs, studies treatment effect
Good, shock resistance is strong, and the high integration apparatus of stability becomes development trend.
The content of the invention
Goal of the invention：
It is an object of the invention to provide one kind operation and maintenance management are simple, operation is easy, compact-sized, space availability ratio is high
And it is easy to assembly, the impact load of resistance to waterpower ability is strong, and processing water scope is big, stable effluent quality, without extra electric power energy
The solar energy type cold district sanitary sewage disposal integration apparatus of source heated waste water, to solve remote districts, power shortage area
Effective processing of domestic sewage in rural areas and other processing equipment winter low temperature systems can not normal operation or sewage disposal effects
The problem of rate is low, effective the problems such as solving poor mud-water separation poor performance, denitrification effect under low temperature, sludge bulking.
Technical solution：
Solar energy type cold district sanitary sewage disposal integration apparatus, it is characterised in that：Including babinet, the babinet includes lattice
Grid pond, regulating reservoir, bioselection pond, anoxic pond, aerobic tank, MBR ponds, ultraviolet sterilizer, equipment room；
The grid pond bottom is equipped with the first elevator pump, and regulating reservoir bottom is equipped with the second elevator pump, and anoxic pond bottom is equipped with the 3rd
Elevator pump, hollow fiber film assembly is equipped with MBR ponds, and the outlet of the first elevator pump is arranged in regulating reservoir by pipeline, and second carries
The outlet for rising pump is arranged in bioselection pond by pipeline, and bioselection bottom of pond portion passes through pipeline and anoxic pond side-lower entrance phase
Even, the outlet of the 3rd elevator pump is arranged in aerobic tank by pipeline, and crest of weir is equipped between aerobic tank and MBR ponds；
The equipment room includes pneumatic diaphragm pump, MBR self priming pumps, Electromagnetic diaphragm metering pump, medicine-adding bin, air compressor machine, electric autocontrol
Device, by pipeline with being connected inside medicine-adding bin, Electromagnetic diaphragm metering pump outlet is set Electromagnetic diaphragm metering pump entrance by pipeline
In in regulating reservoir；The entrance of MBR self priming pumps is connected by pipeline and hollow fiber film assembly outlet, and the outlet of MBR self priming pumps leads to
Pipeline is crossed with the entrance of ultraviolet sterilizer to be connected；First import of pneumatic diaphragm pump is arranged in aerobic tank by pipeline, pneumatically
Second import of diaphragm pump is arranged in MBR ponds by pipeline, and the water outlet of pneumatic diaphragm pump is arranged in anoxic pond by pipeline；
The primary outlet of air compressor machine connects the air inlet of pneumatic diaphragm pump by pipeline, and second outlet of air compressor machine is connected by pipeline
The micropore aeration pipe being connected in aerobic tank, the 3rd outlet of air compressor machine are connected to the macropore aeration tube in MBR ponds by pipeline；
First elevator pump, the second elevator pump, the 3rd elevator pump, Electromagnetic diaphragm metering pump, MBR self priming pumps and air compressor machine with electrically
Self-con-tained unit is connected by electric wire.
The MBR bottom of pond portion is equipped with sludge reflux pump, and sludge reflux pump discharge is arranged in bioselection pond by pipeline, into
Row sludge reflux；The sludge reflux pump is connected with electric autocontrol device by electric wire.
Immersion heater is equipped with the regulating reservoir, carries out liquid heating.
Vertical mixer is equipped with the top of the anoxic pond, the vertical mixer is connected with electric autocontrol device by electric wire
Connect.
The equipment room further includes solar energy inverter control all-in-one machine and storage battery, and solar energy inverter control all-in-one machine is too
Positive energy plate is located on the outside of babinet, solar energy inverter control all-in-one machine connection storage battery, storage battery connection immersion heater
Power to immersion heater.
The side that the babinet is located at equipment room is equipped with the sliding door entered for people, and casing top, which is located above equipment room, to be set
There is ventilating opening, casing top, which is located above bioselection pond and MBR ponds, is respectively equipped with access hole.
Added with floating stuffing in the aerobic tank.
The grid pond, regulating reservoir, anoxic pond, the bottom in MBR ponds are equipped with blow-down pipe.
A kind of method using the solar energy type cold district sanitary sewage disposal integration apparatus treated sewage, its
It is characterized in that：Method is as follows：Sanitary sewage initially enters grid pond and removes the insoluble suspended matter of bulky grain, then by the first elevator pump
It is promoted in regulating reservoir, is promoted in bioselection pond and screened by the second elevator pump pump by the sewage after regulating water quality water
Cultivate excellent microorganism and handle water pollutant at the same time, then anoxic pond is flowed into by gravity mode, then lifted by the 3rd elevator pump
To aerobic tank, at the same the mixed liquor in aerobic tank, MBR ponds can single-pipeline or dual circuit be back in anoxic pond and carry out denitrogenation
Processing, further optimizing water quality, finally enters in MBR ponds and carries out mud-water separation by plate film assembly, water outlet is by MBR self priming pumps
Extraction.
Advantage and effect：
The present invention solar energy type cold district sanitary sewage disposal integration apparatus, with when can use Improvement type A/O be raw
Thing processing system and MBR film separation systems are combined.Realize modularized design, biological treatment can be carried out according to processing water size
System and the combination of biological treatment system and film separation system mutually switch.Realize the electric autocontrol system of intelligence, easy to operate, dimension
Shield is convenient.For boreal climate, using mature and stable treatment process, and increase immersion heater so that winter goes out
Water is still stablized, and is conducive to optimize the environment.Using photovoltaic generating system, lower operating cost, solve powerup issue from far-off regions.
This equipment uses the form of babinet, mobile flexible, is adapted to the sewage disposal in the regions such as small towns, holiday village.What equipment used
Mixed-liquor return mode is various, and controllability is strong, and denitrification effect is good；And make full use of micro- life that raw water quality has been adapted in raw water
Thing realizes the reinforcing adsorption capacity to suspended matter in raw water；Effectively reduce suction-operated and denitrification of the low temperature to microorganism
Influence, effectively reduce influence of the low temperature to mud-water separation, can meet cold district sanitary sewage qualified discharge or in
Water circulation.
Brief description of the drawings
Fig. 1 is the structure diagram of the embodiment of the present invention；
Fig. 2 is the schematic top plan view of the present invention.
Description of reference numerals：
1st, grid pond；2nd, regulating reservoir；3rd, bioselection pond；4th, anoxic pond；5th, aerobic tank；6th, MBR ponds；7th, ultraviolet sterilizer；8
Equipment room；9th, electric autocontrol device；10th, solar energy inverter control all-in-one machine；11st, storage battery；12nd, pneumatic diaphragm pump；13、MBR
Self priming pump；14th, Electromagnetic diaphragm metering pump；15th, medicine-adding bin；16th, air compressor machine；17th, macropore aeration tube；18th, the first elevator pump；19、
Second elevator pump；20th, vertical mixer；21st, the 3rd elevator pump；22nd, immersion heater；23rd, sludge reflux pump；24、
Micropore aeration pipe；25th, floating stuffing；26th, hollow fiber film assembly；27th, babinet；28th, equipment room sliding door；29th, blow-down pipe；
30th, ventilating opening；31st, access hole；32nd, crest of weir.
Embodiment
The present invention is described further below in conjunction with the accompanying drawings：
As depicted in figs. 1 and 2, solar energy type cold district sanitary sewage disposal integration apparatus, including babinet 27, babinet 27 by
Each side panel and upper and lower plate surround rectangular shape, and each plate is equipped with insulating layer.The babinet 27 includes grid pond 1, regulating reservoir
2nd, bioselection pond 3, anoxic pond 4, aerobic tank 5, MBR ponds 6, ultraviolet sterilizer 7, equipment room 8；1 bottom of grid pond is equipped with
First elevator pump 18,2 bottom of regulating reservoir are equipped with the second elevator pump 19, immersion heater 22 are additionally provided with regulating reservoir 2, into
Row liquid heats, and 4 bottom of anoxic pond is equipped with the 3rd elevator pump 21, and hollow fiber film assembly 26, the first lifting are equipped with MBR ponds 6
The outlet of pump 18 is arranged in regulating reservoir 2 by pipeline, and the outlet of the second elevator pump 19 is arranged in bioselection pond 3 by pipeline,
3 bottom of bioselection pond is connected by pipeline with 4 side-lower entrance of anoxic pond, and the top of anoxic pond 4 is equipped with vertical mixer
20, mixed liquor stirring is carried out, keeps certain dissolved oxygen content in anoxic pond 4, the outlet of the 3rd elevator pump 21 is arranged on by pipeline
In oxygen pond 5, added with floating stuffing 25 in aerobic tank 5, crest of weir 32 is equipped between aerobic tank 5 and MBR ponds 6, mixed liquor in aerobic tank 5
Pass through 32 overflow of crest of weir to MBR ponds 6；6 bottom of MBR ponds is equipped with sludge reflux pump 23, and sludge reflux pump 23 is exported to be set by pipeline
In in bioselection pond 3, sludge reflux is carried out；Grid pond 1, regulating reservoir 2, anoxic pond 4, the bottom in MBR ponds 6 are equipped with blow-down pipe
29, when plant maintenance is with overhauling, blow-down pipe 29 is opened, discharges the sewage in pond body.The equipment room 8 includes pneumatic diaphragm pump
12nd, MBR self priming pumps 13, Electromagnetic diaphragm metering pump 14, medicine-adding bin 15, air compressor machine 16, electric autocontrol device 9.Electromagnetic diaphragm is measured
14 entrances are pumped by pipeline with the inside of medicine-adding bin 15 to be connected, the outlet of Electromagnetic diaphragm metering pump 14 is arranged in regulating reservoir 2 by pipeline,
Electromagnetic diaphragm metering pump 14 is used for dosing；The entrance of MBR self priming pumps 13 is connected by pipeline and the outlet of hollow fiber film assembly 26,
The outlet of MBR self priming pumps 13 is connected by pipeline with the entrance of ultraviolet sterilizer 7；First import of pneumatic diaphragm pump 12 passes through
Pipeline is arranged in aerobic tank 5, and second import of pneumatic diaphragm pump 12 is arranged in MBR ponds 6 by pipeline, pneumatic diaphragm pump 12
Water outlet is arranged in anoxic pond 4 by pipeline；The mixed-liquor return of various ways is carried out, it is mixed in aerobic tank 5 or MBR ponds 6
Anoxic pond 4 can be individually back to by closing liquid, the mixed liquor in aerobic tank 5 and MBR ponds 6 can also according to water quality situation according to
Certain ratio is back to anoxic pond 4.The primary outlet of air compressor machine 16 connects the air inlet of pneumatic diaphragm pump 12 by pipeline,
Power is provided for pneumatic diaphragm pump 12；Second outlet of air compressor machine 16 is connected to the micro-pore aeration in aerobic tank 5 by pipeline
Pipe 24, to being supplied oxygen in aerobic tank 5；The macropore that 3rd outlet of air compressor machine 16 is connected to by pipeline in MBR ponds 6 is aerated
Pipe 17, washes away hollow fiber film assembly 26 in MBR ponds 6；Equipment room 8 further includes 10 He of solar energy inverter control all-in-one machine
Storage battery 11, the solar panels of solar energy inverter control all-in-one machine 10 are located at the outside of babinet 27, solar energy inverter control all-in-one machine
10 connection storage batteries 11, convert the solar into electric energy and are stored into storage battery 11, storage battery 11 connects immersion heater
22, power to immersion heater 22.The side that babinet 27 is located at equipment room 8 is equipped with the sliding door 28 entered for people, case
The top of body 27 is equipped with ventilating opening 30 positioned at the top of equipment room 8, and the top of babinet 27 is located at bioselection pond 3 and the top of MBR ponds 6 respectively
Equipped with access hole 31.
It is MBR self priming pumps 13, Electromagnetic diaphragm metering pump 14, air compressor machine 16, the first elevator pump 18, the second elevator pump 19, vertical
Mixer 20, the 3rd elevator pump 21 and sludge reflux pump 23 are connected with electric autocontrol device 9 by electric wire.Electric autocontrol device
9 can realize equipment automatic control.
The characteristics of for country sewage, set floating stuffing 25 using 2 regulating water quality water of regulating reservoir, in aerobic tank 5 and be used for
Aufwuch, MBR ponds 6 are interior to be equipped with core component hollow fiber film assembly 26, and ultraviolet sterilizer 7 is evacuated to using MBR self priming pumps 13,
Ultraviolet sterilizer 7 goes the pathogen in water removal.Using air compressor machine 16 to being supplied oxygen in aerobic tank 5, to hollow fibre in MBR ponds 6
Dimension membrane module 26 is washed away, and sludge reflux pump 23 is equipped with MBR ponds 6 and carries out sludge reflux, equipment room 8 is equipped with pneumatic diaphragm pump
12 carry out mixed-liquor returns, and the top of anoxic pond 4 is equipped with vertical mixer 20, carries out liquid agitation, realize preferable nitrification and instead
Nitrification, so that qualified discharge or Treated sewage reusing.
Immersion heater 22 is equipped with regulating reservoir 2, carries out liquid heating, to ensure normal in the winter time in car body transport
OK.The storage battery 11 and solar control integrated machine for reverse conversion 10 for coordinating solar panel are equipped with equipment room 8, it is ensured that remote
Equipment normal operation under the inconvenient and unexpected power down mode of regional electricity consumption.
It is as follows using the method for solar energy type cold district sanitary sewage disposal integration apparatus treated sewage, method：It is raw
Sewage living initially enters grid pond 1 and removes the insoluble suspended matter of bulky grain, then is promoted to by the first elevator pump 18 in regulating reservoir 2,
The excellent micro- life of screening and culturing in bioselection pond 3 is promoted to by the second elevator pump pump 19 by the sewage after regulating water quality water
Thing handles water pollutant at the same time, then flows into anoxic pond 4 by gravity mode, then is promoted to aerobic tank 5 by the 3rd elevator pump 21,
At the same time mixed liquor in aerobic tank 5, MBR ponds 6 can single-pipeline or dual circuit be back in anoxic pond 4 and carry out denitrogenation processing,
Further optimizing water quality, finally enters in MBR ponds 6 and carries out mud-water separation by plate film assembly 26, water outlet is by MBR self priming pumps 13
Extraction.
Obviously, the above embodiment of the present invention is only intended to clearly illustrate example of the present invention, and is not pair
The restriction of embodiments of the present invention, for those of ordinary skill in the field, may be used also on the basis of the above description
To make other various forms of changes or variation, all embodiments can not be exhaustive here, it is every to belong to this hair
Row of the obvious changes or variations that bright technical solution is extended still in protection scope of the present invention.
Claims (9)
1. solar energy type cold district sanitary sewage disposal integration apparatus, it is characterised in that：Including babinet（27）, the babinet
（27）Including grid pond（1）, regulating reservoir（2）, bioselection pond（3）, anoxic pond（4）, aerobic tank（5）, MBR ponds（6）, ultraviolet kill
Bacterium device（7）, equipment room（8）；
The grid pond（1）Bottom is equipped with the first elevator pump（18）, regulating reservoir（2）Bottom is equipped with the second elevator pump（19）, anoxic
Pond（4）Bottom is equipped with the 3rd elevator pump（21）, MBR ponds（6）It is interior to be equipped with hollow fiber film assembly（26）, the first elevator pump（18）'s
Outlet is arranged on regulating reservoir by pipeline（2）It is interior, the second elevator pump（19）Outlet bioselection pond is arranged on by pipeline（3）It is interior,
Bioselection pond（3）Bottom passes through pipeline and anoxic pond（4）Side-lower entrance is connected, the 3rd elevator pump（21）Outlet pass through pipe
Road is arranged on aerobic tank（5）It is interior, aerobic tank（5）With MBR ponds（6）Between be equipped with crest of weir（32）；
The equipment room（8）Including pneumatic diaphragm pump（12）, MBR self priming pumps（13）, Electromagnetic diaphragm metering pump（14）, medicine-adding bin
（15）, air compressor machine（16）, electric autocontrol device（9）, Electromagnetic diaphragm metering pump（14）Entrance passes through pipeline and medicine-adding bin（15）It is interior
Portion is connected, Electromagnetic diaphragm metering pump（14）Outlet is arranged on regulating reservoir by pipeline（2）It is interior；MBR self priming pumps（13）Entrance pass through
Pipeline and hollow fiber film assembly（26）Outlet connection, MBR self priming pumps（13）Outlet pass through pipeline and ultraviolet sterilizer（7）'s
Entrance is connected；Pneumatic diaphragm pump（12）First import aerobic tank is arranged on by pipeline（5）It is interior, pneumatic diaphragm pump（12）
Two imports are arranged on MBR ponds by pipeline（6）It is interior, pneumatic diaphragm pump（12）Water outlet anoxic pond is arranged on by pipeline（4）It is interior；
Air compressor machine（16）Primary outlet pneumatic diaphragm pump is connected by pipeline（12）Air inlet, air compressor machine（16）Second go out
Mouth is connected to aerobic tank by pipeline（5）In micropore aeration pipe（24）, air compressor machine（16）The 3rd outlet by pipeline company
It is connected to MBR ponds（6）In macropore aeration tube（17）；
First elevator pump（18）, the second elevator pump（19）, the 3rd elevator pump（21）, Electromagnetic diaphragm metering pump（14）, MBR self priming pumps
（13）And air compressor machine（16）With electric autocontrol device（9）Connected by electric wire.
2. solar energy type cold district sanitary sewage disposal integration apparatus according to claim 1, it is characterised in that：Institute
State MBR ponds（6）Bottom is equipped with sludge reflux pump（23）, sludge reflux pump（23）Outlet is arranged on bioselection pond by pipeline（3）
It is interior, carry out sludge reflux；The sludge reflux pump（23）With electric autocontrol device（9）Connected by electric wire.
3. solar energy type cold district sanitary sewage disposal integration apparatus according to claim 1, it is characterised in that：Institute
State regulating reservoir（2）It is interior to be equipped with immersion heater（22）, carry out liquid heating.
4. solar energy type cold district sanitary sewage disposal integration apparatus according to claim 1, it is characterised in that：Institute
State anoxic pond（4）Top is equipped with vertical mixer（20）, the vertical mixer（20）With electric autocontrol device（9）Pass through electric wire
Connection.
5. solar energy type cold district sanitary sewage disposal integration apparatus according to claim 1, it is characterised in that：Institute
State equipment room（8）Further include solar energy inverter control all-in-one machine（10）And storage battery（11）, solar energy inverter control all-in-one machine
（10）Solar panels be located at babinet（27）Outside, solar energy inverter control all-in-one machine（10）Connect storage battery（11）, storage battery
（11）Connect immersion heater（22）To immersion heater（22）Power supply.
6. solar energy type cold district sanitary sewage disposal integration apparatus according to claim 1, it is characterised in that：Institute
State babinet（27）Positioned at equipment room（8）Side be equipped with for people enter sliding door（28）, babinet（27）Top is located at equipment room
（8）Top is equipped with ventilating opening（30）, babinet（27）Top is located at bioselection pond（3）With MBR ponds（6）Top is respectively equipped with maintenance
Mouthful（31）.
7. solar energy type cold district sanitary sewage disposal integration apparatus according to claim 1, it is characterised in that：Institute
State aerobic tank（5）It is interior added with floating stuffing（25）.
8. solar energy type cold district sanitary sewage disposal integration apparatus according to claim 1, it is characterised in that：Institute
State grid pond（1）, regulating reservoir（2）, anoxic pond（4）, MBR ponds（6）Bottom be equipped with blow-down pipe（29）.
9. one kind uses solar energy type cold district sanitary sewage disposal integration apparatus treated sewage as claimed in claim 1
Method, it is characterised in that：Method is as follows：Sanitary sewage initially enters grid pond（1）The insoluble suspended matter of bulky grain is removed, then
By the first elevator pump（18）It is promoted to regulating reservoir（2）It is interior, pumped by the sewage after regulating water quality water by the second elevator pump
（19）It is promoted to bioselection pond（3）The middle excellent microorganism of screening and culturing handles water pollutant at the same time, then passes through gravity mode
Flow into anoxic pond（4）, then by the 3rd elevator pump（21）It is promoted to aerobic tank（5）, while in aerobic tank（5）, MBR ponds（6）In
Mixed liquor can single-pipeline or dual circuit be back to anoxic pond（4）Middle carry out denitrogenation processing, further optimizing water quality, finally enters
MBR ponds（6）It is interior to pass through plate film assembly（26）Mud-water separation is carried out, water outlet is by MBR self priming pumps（13）Extraction.
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