CN106927645A - A kind of sewage disposal system and sewage water treatment method - Google Patents
A kind of sewage disposal system and sewage water treatment method Download PDFInfo
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- CN106927645A CN106927645A CN201710303298.7A CN201710303298A CN106927645A CN 106927645 A CN106927645 A CN 106927645A CN 201710303298 A CN201710303298 A CN 201710303298A CN 106927645 A CN106927645 A CN 106927645A
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- sewage
- reverse osmosis
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- disposal system
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F9/00—Multistage treatment of water, waste water or sewage
-
- 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
-
- 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
-
- 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
- C02F1/52—Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2101/00—Nature of the contaminant
- C02F2101/10—Inorganic compounds
- C02F2101/16—Nitrogen compounds, e.g. ammonia
-
- 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
- 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
- C02F3/28—Anaerobic digestion processes
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F5/00—Softening water; Preventing scale; Adding scale preventatives or scale removers to water, e.g. adding sequestering agents
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- 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)
Abstract
The invention provides a kind of sewage disposal system and sewage water treatment method, including pretreatment unit, anaerobic biochemical treatment unit, film biological processing unit, pliable cell, reverse osmosis units and the network pipe type reverse osmosis units being sequentially connected.Leachate collection hole is burned after waste incineration by after burning liquid collection, sequentially pass through pretreatment unit, anaerobic biochemical treatment unit, film biological processing unit, pliable cell, reverse osmosis units and network pipe type reverse osmosis units, can obtain filter water, qualified discharge standard is reached by the filter water after sewage disposal system treatment, and obtain concentrate by reverse osmosis units, condensed liquid is after network pipe type reverse osmosis units are further concentrated, can be used for flyash curing, lime slurrying, cooling of furnace slag treatment, sewage can be processed utilization completely, and unharmful substance after treatment, more environmental protection.
Description
Technical field
The present invention relates to water-treatment technology field, more particularly to a kind of sewage disposal system and sewage water treatment method.
Background technology
Sewage in garbage incinerating power plant production process produced by each workshop section needs to enter by after collection, first having to
Dump pit is stored up, so that rubbish heap fermentation, Leachate site are smoothly derived, improves refuse thermal value, it is ensured that when equipment breakdown or maintenance
Rubbish can be still received, certain adjustment effect is played.Percolate and discharging platform flushing water that rubbish is produced during storing up
Deng by environmental impact assessment requirement, treatment up to standard in the lump is needed.At present, to reach strict environmental impact assessment requirement, percolate treatment is more employed
" pretreatment+biological treatment+bi-membrane method (NF+RO) " combined treatment process, its advantage be outlet effect it is good, can qualified discharge, account for
Ground area is small；But there is also that investment is big, operating cost is high, film easily pollutes and blocks, water rate is relatively low (70%), produce a large amount of
The problems such as (30% or so) film concentrate.Wherein, dope problem is current most scabrous problem.The settling mode of current dope
Main to have thermal evaporation techniques and return spray incineration technology, the two has that operation cost is too high.
The flue gas of garbage incinerating power plant need to carry out depickling and cooling treatment, and depickling is with calcium hydroxide absorption flue gas
The sour gas such as sulfide, hydrogen chloride, cooling treatment.Semidry method depickling is the calcium hydroxide slurry using concentration about 15% to cigarette
Gas carries out depickling and cooling simultaneously, during need to expend a large amount of water.The ash collected through smoke processing system after waste incineration claims
Be flying dust, flying dust belongs to hazardous waste, therefore after needing stabilized treatment, can just be transported to Landfills landfill stabilization.Using
The method stabilization flying dust of cement+chelating composite curing, during need also exist for adding the humidification water of flying dust amount 30% to 35%.
The content of the invention
Technical problem solved by the invention is to provide a kind of sewage disposal system simple to operate, good sewage processing effect
System and sewage water treatment method.
In order to solve the above technical problems, the invention provides a kind of sewage disposal system, including the pretreatment being sequentially connected
Unit, anaerobic biochemical treatment unit, film biological processing unit, pliable cell, reverse osmosis units and network pipe type reverse osmosis units.
Further, the anaerobic biochemical treatment unit includes the sewage sludge reactor, the three-phase that set gradually from bottom to top
Separator and air chamber, the bottom of the sewage sludge reactor are connected with the pretreatment unit, the top of the sewage sludge reactor
It is connected with the film biological processing unit, the bottom of the sewage sludge reactor is provided with mud discharging mouth.
Further, the film biological processing unit includes that be connected with the anaerobic biochemical treatment unit first is biological
Denitrogenation processing device and the second biological denitrificaion processor being connected with the first biological denitrificaion processor, described second is biological de-
Nitrogen processor is connected with the pliable cell.
Further, the first biological denitrificaion processor and the second biological denitrificaion processor are respectively first and penetrate
Stream aerator and the second jet aerator.
Further, it is provided with tubular type film unit between the film biological processing unit and the pliable cell.
Further, the pretreatment unit includes transfer shares grid area and the coagulation that is connected with the grid area of transferring shares
Settling zone, the coagulating sedimentation area is connected with the anaerobic biochemical treatment unit；The output end in the coagulating sedimentation area is also connected with
There is sewage regulatory region.
Further, the pliable cell include the chemical reactor that is connected with the film biological processing unit and with
The connected cross-current type tubular type film filter of the chemical reactor, the cross-current type tubular type film filter and the reverse osmosis units
It is connected.
Further, the reverse osmosis units include counter-infiltration pipe and the counter-infiltration being arranged in the counter-infiltration pipe
Film, the pore size filter of the reverse osmosis membrane is 0.05 to 0.15 nanometer.
Further, the network pipe type reverse osmosis units include pressure vessel and are arranged in the pressure vessel
Membrane component；The membrane component includes water inlet filter, some diaphragms and product water filter；Every two diaphragms with it is described product water every
Netcom crosses laser welding and forms film pad, and every film pad separated by grid of intaking with the film pad, multi-disc film pad and the water inlet
Spiral rolls to form the membrane component grid successively.
Present invention also offers a kind of sewage water treatment method, including sewage disposal system as described above, methods described bag
Include following steps：
Sewage is pre-processed；
Pretreated sewage is carried out into anaerobic biochemical treatment；
Carry out film biological treatment；
Sewage after film biological treatment is softened；
Sewage after softening is carried out into reverse-osmosis treated；
Sewage after reverse-osmosis treated is carried out into network pipe type reverse-osmosis treated；
Obtain filter water.
Sewage disposal system of the invention, after leachate collection hole is burned after waste incineration by burning liquid collection, passes through successively
Cross pretreatment unit, anaerobic biochemical treatment unit, film biological processing unit, pliable cell, reverse osmosis units and network pipe type anti-
Permeation unit, you can obtain filter water, reaches qualified discharge standard, and pass through by the filter water after sewage disposal system treatment
Reverse osmosis units obtain concentrate, and condensed liquid can be used for flying dust and consolidate after network pipe type reverse osmosis units are further concentrated
Change, lime slurrying, cooling of furnace slag treatment, sewage can be processed unharmful substance, more ring after utilization, and treatment completely
Protect.
Brief description of the drawings
Fig. 1 is the schematic diagram of sewage disposal system of the invention；
Fig. 2 is the structure chart of sewage disposal system of the invention；
Fig. 3 is the schematic diagram of the anaerobic biochemical treatment unit of sewage disposal system of the invention；
Fig. 4 is the schematic diagram of the pliable cell of sewage disposal system of the invention；
Fig. 5 is the schematic diagram of the network pipe type reverse osmosis units of sewage disposal system of the invention；
Fig. 6 is the flow chart of sewage water treatment method of the invention；
Marked in figure：Pretreatment unit 1, grid area 11 of transferring shares, coagulating sedimentation area 12, sewage regulatory region 13, anaerobism life
Change processing unit 2, sewage sludge reactor 21, three phase separator 22, air chamber 23, film biological processing unit 3, the treatment of the first biological denitrificaion
Device 31, the second biological denitrificaion processor 32, pliable cell 4, chemical reactor 41, cross-current type tubular type film filter 42, counter-infiltration
Unit 5, network pipe type reverse osmosis units 6, pressure vessel 61, membrane component 62, tubular type film unit 7.
Specific embodiment
Embodiments of the present invention are described below in detail, the example of the implementation method is shown in the drawings, wherein ad initio
Same or similar element or element with same or like function are represented to same or similar label eventually.Below by ginseng
The embodiment for examining Description of Drawings is exemplary, it is intended to for explaining the present invention, and be not considered as limiting the invention.
As shown in Figures 1 to 5, the present embodiment provides a kind of sewage disposal system, including the pretreatment unit being sequentially connected
1st, anaerobic biochemical treatment unit 2, film biological processing unit 3, pliable cell 4, reverse osmosis units 5 and network pipe type reverse osmosis units
6.After leachate collection hole is burned after waste incineration by burning liquid collection, pretreatment unit 1, anaerobic biochemical treatment list are sequentially passed through
Unit 2, film biological processing unit 3, pliable cell 4, reverse osmosis units 5 and network pipe type reverse osmosis units 6, you can filtered
Water, reaches qualified discharge standard, and concentrated by reverse osmosis units 5 by the filter water after sewage disposal system treatment
Liquid, condensed liquid can be used for flyash curing, lime slurrying, slag cold after network pipe type reverse osmosis units 6 are further concentrated
But process, sewage can be processed unharmful substance after utilization, and treatment completely, more environmental protection.
The sewage disposal system to the present embodiment is described in further detail below.
Pretreatment unit 1 includes transfer shares grid area 11 and the coagulating sedimentation area 12 that is connected with grid area 11 of transferring shares, coagulation
Settling zone 12 is connected with anaerobic biochemical treatment unit 2；The output end in coagulating sedimentation area 12 is also associated with sewage regulatory region 13.Specifically
, grid area 11 of transferring shares can be rotary drum mechanical grille, and drum screen is made by grid gap by grid sheet, and accessing pending water is from grid
Flowed into before basket, by grid filtration, flow to basin outlet, grid slag is trapped within grid face, and the water-head inside and outside grid reaches one
During definite value, the rotation tooth harrow revolution installed on center shaft is removed contamination, when scarfing cinder tooth harrow takes off dirt the position of collection to grid basket summit
When, start slag dumping, the filter residue after dehydration is squeezed, solid content is up to 25% to 45%, it is possible to reduce outward transport expense and prevent two
Secondary pollution.In coagulating sedimentation area 12, in the presence of coagulant, colloid and fine suspension in waste water is set to be condensed into flocculation
Body, is then separated off.
Anaerobic biochemical treatment unit 2 include set gradually from bottom to top sewage sludge reactor 21, three phase separator 22 and
Air chamber 23, the bottom of sewage sludge reactor 21 is connected with pretreatment unit 1, top and the film biological processing unit of sewage sludge reactor 21
3 are connected, and the bottom of sewage sludge reactor 21 is provided with mud discharging mouth.Using three phase separator 22, good gas-solid-liquid is not only ensure that
Separating effect, and, good integrity strong with anticorrosive property, the features such as air-tightness is strong, and structure is simpler.Sewage sludge reactor
In 21, the sludge being precipitated on skew wall slides back to along skew wall, makes the substantial amounts of sludge of accumulation in sewage sludge reactor 21, is separated with sludge
Treatment water outlet afterwards is overflowed from the downflow weir top of sewage sludge reactor 21, is then discharged out.
Film biological processing unit 3 include the first biological denitrificaion processor 31 for being connected with anaerobic biochemical treatment unit 2 and
The second biological denitrificaion processor 32 being connected with the first biological denitrificaion processor 31, the second biological denitrificaion processor 32 is single with softening
Unit 4 is connected.The characteristics of percolate ammonia nitrogen concentration is high, treatment water outlet ammonia nitrogen index is strict, is processed using the first biological denitrificaion
The biological denitrificaion processor 32 of device 31 and second is processed, and by the regulation of the conditions such as carbon-nitrogen ratio, dissolved oxygen, PH, temperature, is protected
The effect of denitrogenation is demonstrate,proved.Using secondary reinforcement denitrification process, the removal effect to ammonia nitrogen and total nitrogen material is strengthened.
First biological denitrificaion processor 31 and the second biological denitrificaion processor 32 are respectively the first jet aerator and second
Jet aerator；So, it is ensured that the coefficient of oxygen utilization of system is more than 35%, system energy consumption is saved.
Tubular type film unit 7 is provided between film biological processing unit 3 and pliable cell 4.The 7 pairs of micro- lifes of activity of tubular type film unit
The complete crown_interception of thing makes the activated sludge concentration upper limit of biochemical system be greatly enhanced.
Pliable cell 4 include the chemical reactor 41 that is connected with film biological processing unit 3 and with the phase of chemical reactor 41
Cross-current type tubular type film filter 42 even, cross-current type tubular type film filter 42 is connected with reverse osmosis units 5.Pliable cell 4 can be with
Deliming, magnesium, silicon, fluorine, barium, strontium are removed in softening.After cross-current type tubular type film filter 42 is filtered, extraordinary water outlet water can be reached
Matter, instead of traditional sedimentation or clarification process.
Reverse osmosis units 5 include counter-infiltration pipe and the reverse osmosis membrane being arranged in the counter-infiltration pipe, reverse osmosis membrane
Pore size filter is 0.05 to 0.15 nanometer；Preferably, the pore size filter of reverse osmosis membrane is 0.1 nanometer；The cutting of reverse osmosis membrane point
Son amount grade is that 20D, i.e. the nanofiltration aperture of reverse osmosis membrane 0.1 can ensure that material grainses of the film to molecular weight more than 20D have
More than 90% clearance.
Network pipe type reverse osmosis units 6 include pressure vessel 61 and the membrane component 62 being arranged in pressure vessel 61；Membrane element
Part 62 includes water inlet filter, some diaphragms and product water filter；Every two diaphragms pass through Laser Welding with the product water filter
Connect to form film pad, every film pad is separated by grid of intaking with the film pad, multi-disc film pad and the water inlet grid spiral successively
Roll to form the membrane component.Membrane component 62 combines the advantage on open runner and wound element design, greatly optimizes
The effective area of water inlet filter and membrane component 62, shortens product water channel length, reduces the product water channel pressure loss；Can use up
Amount keeps the different places water-carrying capacity of membrane component 62 same or similar.
As shown in fig. 6, present invention also offers a kind of sewage water treatment method, including sewage disposal system as described above,
The described method comprises the following steps：
Sewage is pre-processed；
Pretreated sewage is carried out into anaerobic biochemical treatment；
Carry out film biological treatment；
Sewage after film biological treatment is softened；
Sewage after softening is carried out into reverse-osmosis treated；
Sewage after reverse-osmosis treated is carried out into network pipe type reverse-osmosis treated；
Obtain filter water.
Sewage disposal system of the invention, after leachate collection hole is burned after waste incineration by burning liquid collection, passes through successively
Cross pretreatment unit 1, anaerobic biochemical treatment unit 2, film biological processing unit 3, pliable cell 4, reverse osmosis units 5 and webmaster
Formula reverse osmosis units 6, you can obtain filter water, qualified discharge standard is reached by the filter water after sewage disposal system treatment,
And concentrate is obtained by reverse osmosis units 5, condensed liquid can be used after network pipe type reverse osmosis units 6 are further concentrated
In flyash curing, lime slurrying, cooling of furnace slag treatment, sewage can completely be processed unharmful substance after utilization, and treatment, more
Plus environmental protection.
The above, is only highly preferred embodiment of the present invention, and any formal limitation is not made to the present invention, is appointed
What those of ordinary skill in the art, in the case where technical solution of the present invention ambit is not departed from, using in the method for the disclosure above
Appearance makes many possible variations and modification to technical solution of the present invention, belongs to protective scope of the claims.
Claims (10)
1. a kind of sewage disposal system, it is characterised in that：Including be sequentially connected pretreatment unit, anaerobic biochemical treatment unit,
Film biological processing unit, pliable cell, reverse osmosis units and network pipe type reverse osmosis units.
2. sewage disposal system as claimed in claim 1, it is characterised in that：The anaerobic biochemical treatment unit is included from lower
On the sewage sludge reactor, three phase separator and the air chamber that set gradually, the bottom of the sewage sludge reactor and the pretreatment are single
Unit is connected, and the top of the sewage sludge reactor is connected with the film biological processing unit, and the bottom of the sewage sludge reactor is set
There is mud discharging mouth.
3. sewage disposal system as claimed in claim 1, it is characterised in that：The film biological processing unit includes detesting with described
The first connected biological denitrificaion processor of oxygen biochemical treatment unit and be connected with the first biological denitrificaion processor second
Biological denitrificaion processor, the second biological denitrificaion processor is connected with the pliable cell.
4. sewage disposal system as claimed in claim 3, it is characterised in that：The first biological denitrificaion processor and described
Two biological denitrificaion processors are respectively the first jet aerator and the second jet aerator.
5. sewage disposal system as claimed in claim 1, it is characterised in that：The film biological processing unit softens list with described
Tubular type film unit is provided between unit.
6. sewage disposal system as claimed in claim 3, it is characterised in that：The pretreatment unit include transfer shares grid area with
And the coagulating sedimentation area being connected with the grid area of transferring shares, the coagulating sedimentation area is connected with the anaerobic biochemical treatment unit；
The output end in the coagulating sedimentation area is also associated with sewage regulatory region.
7. sewage disposal system as claimed in claim 1, it is characterised in that：The pliable cell is included at biological with the film
The connected chemical reactor of reason unit and the cross-current type tubular type film filter being connected with the chemical reactor, the cross-current type
Tubular type film filter is connected with the reverse osmosis units.
8. sewage disposal system as claimed in claim 1, it is characterised in that：The reverse osmosis units include counter-infiltration pipe and
The reverse osmosis membrane in the counter-infiltration pipe is arranged at, the pore size filter of the reverse osmosis membrane is 0.05 to 0.15 nanometer.
9. sewage disposal system as claimed in claim 1, it is characterised in that：The network pipe type reverse osmosis units hold including pressure
Device and the membrane component being arranged in the pressure vessel；The membrane component include water inlet filter, some diaphragms and produce water every
Net；Every two diaphragms form film pad with the product water filter by laser welding, and every film pad is by grid and the institute of intaking
The separation of film pad is stated, spiral rolls to form the membrane component successively for multi-disc film pad and the water inlet grid.
10. a kind of sewage water treatment method, it is characterised in that including the sewage disposal system as described in claim 1 to 9 any one
System, the described method comprises the following steps：
Sewage is pre-processed；
Pretreated sewage is carried out into anaerobic biochemical treatment；
Carry out film biological treatment；
Sewage after film biological treatment is softened；
Sewage after softening is carried out into reverse-osmosis treated；
Sewage after reverse-osmosis treated is carried out into network pipe type reverse-osmosis treated；
Obtain filter water.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201710303298.7A CN106927645A (en) | 2017-05-03 | 2017-05-03 | A kind of sewage disposal system and sewage water treatment method |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201710303298.7A CN106927645A (en) | 2017-05-03 | 2017-05-03 | A kind of sewage disposal system and sewage water treatment method |
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| CN106927645A true CN106927645A (en) | 2017-07-07 |
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| CN201710303298.7A Pending CN106927645A (en) | 2017-05-03 | 2017-05-03 | A kind of sewage disposal system and sewage water treatment method |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108928877A (en) * | 2018-07-23 | 2018-12-04 | 北京市环境卫生设计科学研究所 | A method of utilizing slag treatment rubbish concentrate |
| CN112744956A (en) * | 2021-01-27 | 2021-05-04 | 浦湘生物能源股份有限公司 | Full-scale treatment process and treatment system for reverse osmosis concentrated solution of refuse leachate of incineration plant |
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| CN101219842A (en) * | 2008-02-02 | 2008-07-16 | 张大群 | Technique and equipment for recycling leachate of garbage |
| CN102167479A (en) * | 2011-03-22 | 2011-08-31 | 江苏久吾高科技股份有限公司 | A landfill leachate treatment process |
| CN103864240A (en) * | 2014-01-07 | 2014-06-18 | 杭州深瑞水务有限公司 | Pipe network type garbage leachate processing device |
| CN104496079A (en) * | 2014-12-23 | 2015-04-08 | 北京桑德环境工程有限公司 | Treatment method for garbage leachate membrane concentrated solution |
| CN105417827A (en) * | 2015-12-31 | 2016-03-23 | 杭州深瑞水务有限公司 | Chemical waste water treatment device and method |
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|---|---|---|---|---|
| CN101219842A (en) * | 2008-02-02 | 2008-07-16 | 张大群 | Technique and equipment for recycling leachate of garbage |
| CN102167479A (en) * | 2011-03-22 | 2011-08-31 | 江苏久吾高科技股份有限公司 | A landfill leachate treatment process |
| CN103864240A (en) * | 2014-01-07 | 2014-06-18 | 杭州深瑞水务有限公司 | Pipe network type garbage leachate processing device |
| CN104496079A (en) * | 2014-12-23 | 2015-04-08 | 北京桑德环境工程有限公司 | Treatment method for garbage leachate membrane concentrated solution |
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| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108928877A (en) * | 2018-07-23 | 2018-12-04 | 北京市环境卫生设计科学研究所 | A method of utilizing slag treatment rubbish concentrate |
| CN112744956A (en) * | 2021-01-27 | 2021-05-04 | 浦湘生物能源股份有限公司 | Full-scale treatment process and treatment system for reverse osmosis concentrated solution of refuse leachate of incineration plant |
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Application publication date: 20170707 |