CN105967437A - Constant-temperature integral membrane method reclaimed water reuse equipment - Google Patents
Constant-temperature integral membrane method reclaimed water reuse equipment Download PDFInfo
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- CN105967437A CN105967437A CN201610329794.5A CN201610329794A CN105967437A CN 105967437 A CN105967437 A CN 105967437A CN 201610329794 A CN201610329794 A CN 201610329794A CN 105967437 A CN105967437 A CN 105967437A
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- embrane method
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- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims abstract description 56
- 239000012528 membrane Substances 0.000 title claims abstract description 40
- 238000000034 method Methods 0.000 title claims abstract description 31
- 239000010865 sewage Substances 0.000 claims abstract description 40
- 238000004659 sterilization and disinfection Methods 0.000 claims abstract description 23
- 230000000694 effects Effects 0.000 claims abstract description 13
- 230000008569 process Effects 0.000 claims abstract description 9
- 238000013461 design Methods 0.000 claims abstract description 5
- 238000006243 chemical reaction Methods 0.000 claims description 25
- 230000001954 sterilising effect Effects 0.000 claims description 22
- 230000010354 integration Effects 0.000 claims description 19
- 239000011229 interlayer Substances 0.000 claims description 7
- 230000009471 action Effects 0.000 claims description 6
- 230000000813 microbial effect Effects 0.000 claims description 5
- 238000001223 reverse osmosis Methods 0.000 claims description 5
- 229910000975 Carbon steel Inorganic materials 0.000 claims description 4
- 239000010962 carbon steel Substances 0.000 claims description 4
- 238000011109 contamination Methods 0.000 claims description 4
- 238000004140 cleaning Methods 0.000 claims description 2
- 238000004891 communication Methods 0.000 claims description 2
- 238000009826 distribution Methods 0.000 claims description 2
- 238000001914 filtration Methods 0.000 abstract description 3
- 238000000746 purification Methods 0.000 abstract description 2
- 238000005842 biochemical reaction Methods 0.000 abstract 2
- 239000011248 coating agent Substances 0.000 abstract 1
- 238000000576 coating method Methods 0.000 abstract 1
- 230000029087 digestion Effects 0.000 abstract 1
- 239000002355 dual-layer Substances 0.000 abstract 1
- 239000012535 impurity Substances 0.000 abstract 1
- 238000005516 engineering process Methods 0.000 description 6
- 238000012545 processing Methods 0.000 description 5
- 239000003570 air Substances 0.000 description 3
- 244000005700 microbiome Species 0.000 description 3
- 238000012986 modification Methods 0.000 description 3
- 230000004048 modification Effects 0.000 description 3
- 230000008859 change Effects 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 241000216843 Ursus arctos horribilis Species 0.000 description 1
- 239000012080 ambient air Substances 0.000 description 1
- 238000013459 approach Methods 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000003851 biochemical process Effects 0.000 description 1
- 230000015556 catabolic process Effects 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 238000000354 decomposition reaction Methods 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 238000006731 degradation reaction Methods 0.000 description 1
- 238000004134 energy conservation Methods 0.000 description 1
- 238000003912 environmental pollution Methods 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 238000009413 insulation Methods 0.000 description 1
- 238000002955 isolation Methods 0.000 description 1
- 239000010410 layer Substances 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 230000002906 microbiologic effect Effects 0.000 description 1
- 238000004064 recycling Methods 0.000 description 1
- 230000009467 reduction Effects 0.000 description 1
- 238000004065 wastewater treatment Methods 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- 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
- C02F1/30—Treatment of water, waste water, or sewage by irradiation
- C02F1/32—Treatment of water, waste water, or sewage by irradiation with ultraviolet light
-
- 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
- C02F1/44—Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis
- C02F1/441—Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis by reverse osmosis
-
- 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
- C02F1/44—Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis
- C02F1/442—Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis by nanofiltration
-
- 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
- C02F1/44—Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis
- C02F1/444—Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis by ultrafiltration or microfiltration
-
- 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
- C02F2301/08—Multistage treatments, e.g. repetition of the same process step under different conditions
-
- 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
-
- 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
- C02F3/28—Anaerobic digestion processes
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)
- Separation Using Semi-Permeable Membranes (AREA)
- Physical Water Treatments (AREA)
Abstract
The invention relates to constant-temperature integral membrane method reclaimed water reuse equipment. According to the process flow, an A/A/O coating treatment assembly adopts a design of a dual-layer jacket type shell, and comprises the following internal components: a grating tank, an A/A/O biochemical reaction tank, a membrane component tank, a water source heat pump chamber, a fan chamber, a disinfection tank and the like which are arranged in an integral shell, wherein domestic sewage is pretreated in an external digestion tank and a regulation tank and enters the grating tank, and bulk polluting impurities in the water are removed by the filtering effect of grating; the domestic sewage enters the A/A/O biochemical reaction tank, and multiple polluting indexes in the water are removed by utilizing traditional biochemical effect; the sewage with greatly reduced biochemical indexes enters the membrane component tank, and is subjected to physical filtering treatment of different grain levels to realize final purification. The equipment has space and cost conservation, the system keeps an excellent efficient and energy-saving operation state, the treated water quality can be effectively improved, and the problems of large floor area and poor effect under a low-temperature climate condition in traditional equipment can be solved.
Description
Technical field
The present invention relates to a kind of equipment for small scall scale city sanitary sewage disposal, specifically at one
The thermostatic type integration embrane method Treated sewage reusing equipment of reason small scall scale city sanitary sewage.
Background technology
Along with water environment pollution increasingly sharpens, sewage disposal industry and technology develop rapidly, at biochemical process sewage
Reason technology becomes better and approaching perfection day by day, but in water, microbial activity is closely related with temperature, and its optimum active temperature is
25-30℃.The tradition integrated water treatment equipment scale of construction is little, is easily affected by ambient temperature, especially north of china in winter gas
Temperature is relatively low, and microbial activity is not enough, causes the effluent quality after processing to exceed standard, it is impossible to maintain continuous print the most sharp
With operation, it is impossible to be also the significant wastage to resource while reducing environmental pollution.
Summary of the invention
It is an object of the invention to the defect for prior art, it is provided that one integrate heat, be incubated with
Biochemical sewage treatment technology normal operation, and the equipment of sustainable offer middle water up to standard are provided, reduce water ring
Environment pollution risk, it is achieved recycling of water resource.
Technical scheme is as follows: a kind of thermostatic type integration embrane method Treated sewage reusing equipment, described in set
For including that jacket type housing, described jacket type enclosure interior are divided into seven rooms, are followed successively by grid in order
Homogenizing pond, anaerobic pond, anoxic pond, Aerobic Pond, comprehensive membrane reaction tank, UV sterilization pool, equipment room, often
Individual indoor location has distinct device, described equipment to include grid, the comprehensive membrane being arranged in grid homogenizing pond
Suction in comprehensive membrane reaction module in reaction tank, the UV sterilization module in UV sterilization pool, equipment room
Pump, water resource heat pump and swinging blower fan.
Further, a kind of thermostatic type integration embrane method Treated sewage reusing equipment as above, wherein, chuck
Sandwich type element is divided into described seven Room with hollow type interlayer dividing plate, and with pipeline communication between each room, sewage is via grid
Filter a section dirt process and successively enter homogenizing pond, anaerobic pond, anoxic pond, Aerobic Pond, pass through microbial cleaning
Effect reduces Shui Zhong contamination index, and under the suction pump swabbing action in equipment room, sewage is through comprehensive membrane
In reaction tank, to realize effluent quality up to standard in the secondary filter effect of comprehensive membrane reaction module, then sterilizes through UV
UV sterilization module disinfective action in pond makes water outlet reach reuse standard, in the process returning in equipment room
Rotatable blower fan is Aerobic Pond, comprehensive membrane reaction tank provides enough air, and water resource heat pump utilizes heat contained by water outlet
Amount carries water temperature in heat makes described equipment in the interlayer of jacket type housing and maintains 25-30 DEG C.
Further, a kind of thermostatic type integration embrane method Treated sewage reusing equipment as above, wherein, described
Jacket type housing use use hollow type sandwich design, two-sided carbon steel one-level anticorrosion structure.
Further, thermostatic type integration embrane method Treated sewage reusing equipment as above, wherein, described comprehensively
Ultrafilter membrane, NF membrane, reverse osmosis membrane it is integrated with in film reaction module.
Further, thermostatic type integration embrane method Treated sewage reusing equipment as above, wherein, described UV
Sterilizing equipment decontaminating apparatus utilizes ultraviolet to sterilize sewage, disinfects.
Further, thermostatic type integration embrane method Treated sewage reusing equipment as above, wherein, described suction
Pump utilizes suction pump swabbing action to complete water circulation.
Further, thermostatic type integration embrane method Treated sewage reusing equipment as above, wherein, described water source
Heat pump draws the heat processed in water and is delivered in the interlayer of jacket type housing, maintains constant temperature for system.
Further, thermostatic type integration embrane method Treated sewage reusing equipment as above, wherein, at described time
Rotatable blower and pipeline, distribution device are Aerobic Pond, comprehensive membrane reaction tank provides enough air.
Beneficial effects of the present invention is as follows:
(1) present invention uses jacket type housing, hollow type sandwich design, two-sided carbon steel one-level anticorrosion structure,
The heat utilizing water resource heat pump to provide in hollow sandwich maintains system stability 25-30 DEG C；
(2) present invention utilizes water resource heat pump can fully draw system warm-up, insulation, water source heat pump units
Process the heat in water, delivered heat to the hollow layer of jacket type housing by heat exchange action, it is achieved
System temperature is constant at 25-30 DEG C；
(3) present invention utilizes the microorganism characteristic that degradation efficiency improves in Suitable ranges so that it is
Winter, summer all grow up under the preference temperature of 25-30 DEG C, realize winter compared to traditional handicraft (outstanding
It is to north cold area) normally, run continuously, sewage treating efficiency promotes 20%；
(4) present invention utilizes water source heat pump technology, with the tail water after process as source, with a small amount of electric energy is
Cost, it is achieved low-temperature heat energy shifts to high-temperature position, compared with air source heat pump, its operational efficiency wants height
Go out 20～60%, energy-conservation 30%.
(5) present invention uses comprehensive membrane reaction module, highly integrated ultrafilter membrane, NF membrane, reverse osmosis
Film, allows originally complicated, the most confusing film processing procedure, is integrated in one, shortens production line；
(6) present invention uses UV sterilization module, utilizes built-in UV sterilizer to carry out processing water
Sterilizing processes, and carries out sewage final purification, is allowed to meet recycle water standard, it is achieved following of the source of water
Ring utilizes；
(7) ensure to keep under microbial activity cryogenic conditions in the winter time optimum state, and then solve low temperature ring
Under border, wastewater treatment efficiency is the best, the problem even stopped transport.
Accompanying drawing explanation
Fig. 1 is thermostatic type integration embrane method Treated sewage reusing device structure schematic diagram of the present invention；
Fig. 2 is hollow sandwich structure chart；
Fig. 3 is that water resource heat pump is heated schematic diagram；
Fig. 4 is present invention process general view.
In figure: (1) jacket type housing, (2) grid homogenizing pond, (3) anaerobic pond, (4) anoxic pond, (5)
Aerobic Pond, (6) comprehensive membrane reaction tank, (7) UV sterilization pool, (8) equipment room, (9) grid, (10) combine
Closing film reaction module, (11) UV sterilization module, (12) suction pump, (13) water resource heat pump, (14) are turned round
Formula blower fan.
Detailed description of the invention
With embodiment, the present invention is described in detail below in conjunction with the accompanying drawings.
As Figure 1-Figure 4, a kind of thermostatic type integration embrane method Treated sewage reusing equipment, including jacket type housing
(1), jacket type housing (1) is internal is divided into seven rooms, respectively grid homogenizing pond (2), anaerobic pond (3),
Anoxic pond (4), Aerobic Pond (5), comprehensive membrane reaction tank (6), UV sterilization pool (7), equipment room (8),
Each indoor location has distinct device, including grid (9), comprehensive membrane reaction module (10), UV sterilization module
(11), suction pump (12), water resource heat pump (13) and swinging blower fan (14).
Jacket type housing (1) is that complete equipment is basic, is also the intermediate portions of practical innovation, jacket type shell
Body uses hollow type sandwich design, two-sided carbon steel one-level anticorrosion structure, its hollow sandwich and water source
Heat pump (13) connects, water resource heat pump supply high temperature circulation water in interlayer, completely cuts off cool ambient air, protects
In card equipment, water temperature maintains 25-30 DEG C.Jacket type housing (1) disposes for internal unit and provides site condition,
By hollow clapboard compartmentation housing is divided into grid homogenizing pond (2), anaerobic pond (3), anoxic pond (4),
Aerobic Pond (5), comprehensive membrane reaction tank (6), UV sterilization pool (7), equipment room (8).Capital equipment grid
(9), comprehensive membrane reaction module (10), UV sterilization module (11), suction pump (12), water resource heat pump (13)
With the differences such as swinging blower fan (14), installation requirement different according to function, be respectively placed in different every
Indoor, are fixed on jacket type housing.
Grid (9) is placed in grid homogenizing pond (2), utilizes the interception function of grizzly bar and automatically returning of rake teeth
Turn, retain the bulk matter contained in sewage, alleviate subsequent processing units load, and in grid homogenizing pond (2)
Inside realize the well-balanced adjustment of water quality, the water yield.
Anaerobic pond (3), anoxic pond (4), Aerobic Pond (5) collectively constitute the biochemical treatment stage, for microorganism
The place that offer of growing up is suitable, by the biochemistry of anaerobe, facultative microbe and aerobic microbiological in pond
Effect, organic contamination index in effective decomposition, reduction sewage.
Comprehensive membrane reaction module (10) is placed in comprehensive membrane reaction tank in (6), be integrated with ultrafilter membrane, NF membrane,
Reverse osmosis membrane, in the sewage of biochemical treatment, contamination index has been greatly reduced, in suction pump (12)
Pass sequentially through the ultrafilter membrane of the descending arrangement in aperture, NF membrane, reverse osmosis membrane under high pressure effect, utilize film
The filtration of equipment, purified treatment further to sewage.
UV sterilization module (11) is placed in UV sterilization pool (7), after using Ultraviolet Disinfection to processing
Sewage carry out sterilizing, disinfect, make water outlet reach Treated sewage reusing standard.
Water resource heat pump (13) connection water outlet and crustless sandwich, with water outlet as source, draw under the effect of electric energy
Heat in water outlet, then heat is inputted crustless sandwich, promote case temperature, the extraneous low temperature of isolation, it is ensured that
Enclosure interior water temperature maintains 25-30 DEG C, it is ensured that the microorganism in biochemical treatment stage is all the time with optimum activity
Work, and then ensure treatment effect.
The various equipment of the present invention, reflection unit are all built in jacket type enclosure interior, and by various device height
Integrated, it is achieved factorial praluction, modularity are installed, effectively reduce floor space, shorten the completion time of project, can
Being built in ground, underground or half the most semi-underground, flexible operation is changeable.The present invention innovates employing jacket type hollow
Housing, with water resource heat pump as power, utilizes overall the heating, be incubated of the heat completion system of water outlet, solves
The problem of operational effect difference under cryogenic conditions in traditional approach, with relatively low input, relatively low operating cost in fact
The four seasons continuous high-efficient of existing equipment runs, it is ensured that water quality reaching standard reuse.
Obviously, those skilled in the art can carry out various change and modification without deviating from this to the present invention
The spirit and scope of invention.So, if these amendments and modification to the present invention belong to right of the present invention
Require and within the scope of equivalent technology, then the present invention is also intended to comprise these change and modification.
Claims (7)
1. a thermostatic type integration embrane method Treated sewage reusing equipment, it is characterised in that: described equipment includes
Jacket type housing (1), described jacket type housing (1) is internal is divided into seven rooms, is followed successively by order
Grid homogenizing pond (2), anaerobic pond (3), anoxic pond (4), Aerobic Pond (5), comprehensive membrane reaction
Pond (6), UV sterilization pool (7), equipment room (8), each indoor location has distinct device, described
Combining in grid (9) that equipment includes being arranged in grid homogenizing pond (2), comprehensive membrane reaction tank (6)
Close the UV sterilization module (11) in film reaction module (10), UV sterilization pool (7), equipment room (8)
Interior suction pump (12), water resource heat pump (13) and swinging blower fan (14).
2. thermostatic type integration embrane method Treated sewage reusing equipment as claimed in claim 1, it is characterised in that:
Jacket type housing (1) is divided into described seven Room, with pipeline communication between each room, sewage with hollow type interlayer dividing plate
Filter via grid (9) cut dirt process successively enter homogenizing pond (2), anaerobic pond (3), anoxic pond (4),
Aerobic Pond (5), reduces Shui Zhong contamination index by microbial cleaning effect, in equipment room (8)
Under suction pump (12) swabbing action, sewage is comprehensive membrane reaction module (10) in comprehensive membrane reaction tank (6)
Secondary filter effect to realize effluent quality up to standard, then the UV sterilization module in UV sterilization pool (7)
(11) disinfective action makes water outlet reach reuse standard, in the process the swinging wind in equipment room (8)
Machine (14) is Aerobic Pond (5), comprehensive membrane reaction tank (6) offer enough air, water resource heat pump (13)
Utilize water outlet institute heat content to carry heat in the interlayer of jacket type housing (1) and make water temperature dimension in described equipment
Hold at 25-30 DEG C.
3. thermostatic type integration embrane method Treated sewage reusing equipment as claimed in claim 1, it is characterised in that:
Described jacket type housing (1), uses hollow type sandwich design, two-sided carbon steel one-level anticorrosion structure.
4. thermostatic type integration embrane method Treated sewage reusing equipment as claimed in claim 1, it is characterised in that:
It is integrated with ultrafilter membrane, NF membrane, reverse osmosis membrane in described comprehensive membrane reaction module (10).
5. thermostatic type integration embrane method Treated sewage reusing equipment as claimed in claim 1, it is characterised in that:
Described UV sterilization module (11) uses built-in Ultraviolet Disinfection to water outlet disinfection.
6. thermostatic type integration embrane method Treated sewage reusing equipment as claimed in claim 1, it is characterised in that:
Electric power, with energy content in water outlet as origin of heat, is converted into hydro-thermal by described water resource heat pump (13), it is ensured that
In jacket type housing (1) interlayer, temperature meets 25-30 DEG C.
7. thermostatic type integration embrane method Treated sewage reusing equipment as claimed in claim 1, it is characterised in that:
Described swinging blower fan (14) is Aerobic Pond (5), comprehensive membrane reaction tank (6) by pipeline, distribution device
Enough air is provided.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610329794.5A CN105967437A (en) | 2016-05-18 | 2016-05-18 | Constant-temperature integral membrane method reclaimed water reuse equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610329794.5A CN105967437A (en) | 2016-05-18 | 2016-05-18 | Constant-temperature integral membrane method reclaimed water reuse equipment |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN105967437A true CN105967437A (en) | 2016-09-28 |
Family
ID=56956396
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201610329794.5A Pending CN105967437A (en) | 2016-05-18 | 2016-05-18 | Constant-temperature integral membrane method reclaimed water reuse equipment |
Country Status (1)
| Country | Link |
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| CN (1) | CN105967437A (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106542674A (en) * | 2016-12-08 | 2017-03-29 | 苏州陈恒织造有限公司 | A kind of distributing rural domestic sewage treatment circulating device |
| CN108046547A (en) * | 2018-01-29 | 2018-05-18 | 武汉都市环保工程技术股份有限公司 | Breed dirty integrated device and system of handling of excrement |
| CN111573993A (en) * | 2020-06-04 | 2020-08-25 | 郑州子然环保科技有限公司 | Accelerate and homothermal industrial sewage treatment device of filtration |
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|---|---|---|---|---|
| CN101117254A (en) * | 2006-08-03 | 2008-02-06 | 东丽纤维研究所（中国）有限公司 | Sewage water reusing integral equipment |
| KR20100030083A (en) * | 2008-09-09 | 2010-03-18 | 김광일 | Sewage treatment system |
| CN201670838U (en) * | 2010-03-03 | 2010-12-15 | 刘军林 | Ground source heat pump biogas digester |
| CN104098227A (en) * | 2014-07-15 | 2014-10-15 | 江南大学 | Method for treating kitchen anaerobic waste water through short-cut nitrification and denitrification |
| CN205740669U (en) * | 2016-05-18 | 2016-11-30 | 北京科林皓华环境科技发展有限责任公司 | A kind of thermostatic type integration embrane method Treated sewage reusing equipment |
-
2016
- 2016-05-18 CN CN201610329794.5A patent/CN105967437A/en active Pending
Patent Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101117254A (en) * | 2006-08-03 | 2008-02-06 | 东丽纤维研究所（中国）有限公司 | Sewage water reusing integral equipment |
| KR20100030083A (en) * | 2008-09-09 | 2010-03-18 | 김광일 | Sewage treatment system |
| CN201670838U (en) * | 2010-03-03 | 2010-12-15 | 刘军林 | Ground source heat pump biogas digester |
| CN104098227A (en) * | 2014-07-15 | 2014-10-15 | 江南大学 | Method for treating kitchen anaerobic waste water through short-cut nitrification and denitrification |
| CN205740669U (en) * | 2016-05-18 | 2016-11-30 | 北京科林皓华环境科技发展有限责任公司 | A kind of thermostatic type integration embrane method Treated sewage reusing equipment |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106542674A (en) * | 2016-12-08 | 2017-03-29 | 苏州陈恒织造有限公司 | A kind of distributing rural domestic sewage treatment circulating device |
| CN108046547A (en) * | 2018-01-29 | 2018-05-18 | 武汉都市环保工程技术股份有限公司 | Breed dirty integrated device and system of handling of excrement |
| CN111573993A (en) * | 2020-06-04 | 2020-08-25 | 郑州子然环保科技有限公司 | Accelerate and homothermal industrial sewage treatment device of filtration |
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Application publication date: 20160928 |
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