CN110282828A - A kind of garbage loading embeading infiltration liquid processing method - Google Patents
A kind of garbage loading embeading infiltration liquid processing method Download PDFInfo
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- CN110282828A CN110282828A CN201910590539.XA CN201910590539A CN110282828A CN 110282828 A CN110282828 A CN 110282828A CN 201910590539 A CN201910590539 A CN 201910590539A CN 110282828 A CN110282828 A CN 110282828A
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- penetrating fluid
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F11/00—Treatment of sludge; Devices therefor
- C02F11/12—Treatment of sludge; Devices therefor by de-watering, drying or thickening
- C02F11/121—Treatment of sludge; Devices therefor by de-watering, drying or thickening by mechanical de-watering
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F11/00—Treatment of sludge; Devices therefor
- C02F11/12—Treatment of sludge; Devices therefor by de-watering, drying or thickening
- C02F11/14—Treatment of sludge; Devices therefor by de-watering, drying or thickening with addition of chemical agents
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F9/00—Multistage treatment of water, waste water or sewage
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/20—Treatment of water, waste water, or sewage by degassing, i.e. liberation of dissolved gases
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/50—Treatment of water, waste water, or sewage by addition or application of a germicide or by oligodynamic treatment
-
- 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
- C02F1/66—Treatment of water, waste water, or sewage by neutralisation; pH adjustment
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F2001/007—Processes including a sedimentation step
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2101/00—Nature of the contaminant
- C02F2101/30—Organic compounds
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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
- C02F2103/00—Nature of the water, waste water, sewage or sludge to be treated
- C02F2103/06—Contaminated groundwater or leachate
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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
- 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
- C02F2303/00—Specific treatment goals
- C02F2303/04—Disinfection
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F3/00—Biological treatment of water, waste water, or sewage
- C02F3/30—Aerobic and anaerobic processes
Abstract
The invention discloses a kind of garbage loading embeadings to permeate liquid processing method, belongs to penetrating fluid processing technology field, the solid impurity removal including S1, penetrating fluid；The ammonia nitrogen removal processing of S2, penetrating fluid；An Anaerobic Treatment of S3, penetrating fluid；The secondary Anaerobic Treatment of S4, penetrating fluid；The Air Exposure of S5, penetrating fluid；S6, infiltration liquid disinfectant；S7, Treatment of Sludge.Anaerobic organic matter inside penetrating fluid is degraded by using secondary Anaerobic Treatment, and secondary Anaerobic Treatment uses UASB reactor and ABR reactor respectively, pole is suitable for processing high-concentration waste water, and sludge loss loss is smaller, is not required to set mixed stirring device, there is no sludge blockage problems, reduce maintenance cost, more economically, the aerobic organic matter in penetrating fluid inside is handled by using SBR Air Exposure mode, to realize, Anaerobic Treatment is combined with an Aerobic Process for Treatment twice, and organic matter is more complete inside processing penetrating fluid.
Description
Technical field
The present invention relates to penetrating fluid processing technology field, in particular to a kind of garbage loading embeading permeates liquid processing method.
Background technique
As China city numbers increase and population increases, municipal refuse is also with sharp increase.According to statistics, annual life
It produces rubbish and has reached 1.5 hundred million tons, it is average to be increased with the speed in 9%/year, wherein untreated rubbish is 7,000,000,000 tons existing, account for
The 8.3% of China soil sum.It is expected that in following 20 years, the discharge amount of solid waste by occupy 85% land, the whole nation
All there is serious refuse pollution in most area.The processing of domestic waste should follow minimizing, recycling, harmless
The principle of change mainly has landfill, compost at present and burns three kinds of processing methods.
Landfill method refers to using natural feature or manual construction, forms certain space, and rubbish filling, compacting, covering are reached
To the purpose of storage.With investing, small, operating cost is low, operation equipment is simple, can handle multiple types for garbage loading embeading processing
Rubbish the features such as.But rubbish, which encounters rainwater weather when landfill, can generate penetrating fluid, penetrating fluid is easy contaminated soil
And the polluted source after earth's surface inflow underground water, therefore the processing of penetrating fluid is the important means of rubbish security landfill.
The processing method multiplicity of landfill leachate, effect are irregular；But in actual application, a certain kind side is only leaned on
Method is difficult to reach processing requirement to handle, it is necessary to using the combination of a variety of methods.The landfill leachate treatment in China at present
Mostly use based on biological method, the group technology supplemented by physical chemistry method, it is excessively high but there are still costs, handle it is unstable, and
The problems such as pollutant removal is not comprehensive enough.
Summary of the invention
The object of the invention is that handling incomplete problem to solve the processing cost of above-mentioned landfill leachate height
And a kind of garbage loading embeading infiltration liquid processing method is provided, secondary Anaerobic Treatment and Aerobic Process for Treatment with microorganism combine, and locate
The advantages of reason better effect, Anaerobic Treatment reduces cost using UASB reactor and ABR reactor.
The present invention is achieved through the following technical solutions above-mentioned purpose, and a kind of garbage loading embeading permeates liquid processing method, including
Following steps:
The solid impurity removal of S1, penetrating fluid: refuse landfill penetrating fluid is collected, and penetrating fluid is first passed through into fine fack and is removed
Internal solid impurity is removed, then is passed through in conditioning tank, the PH of penetrating fluid is improved；
The ammonia nitrogen removal processing of S2, penetrating fluid: the penetrating fluid of the high PH inside step S1 conditioning tank is first passed through into just precipitating, is sunk
Form sediment sludge a small amount of out, and the penetrating fluid on upper layer is passed through stripping tower, carrier gas is passed through in tower body, so that gas-liquid is contacted with each other, makes in water
The free amino molecule of dissolution passes through gas-liquid interface, shifts to gas, to complete the ammonia nitrogen removal processing of penetrating fluid；
An Anaerobic Treatment of S3, penetrating fluid: the penetrating fluid after step S2 ammonia nitrogen removal is passed through up-flow anaerobic sludge blanket
Reactor (UASB), UASB reactor bottom have a Sludge Bed, and the majority of organic pollutants in penetrating fluid is passed through here
Anaerobic fermentation is degraded to methane and carbon dioxide, because of the agitation of water flow and bubble, forms a sludge suspension layer above Sludge Bed,
UASB reactor head has equipped with three phase separator, and to gas, penetrating fluid and the mud granule after separation and fermentation, gas is certainly
The export of UASB reactor head, mud granule slide the Sludge Bed for being settled down to reactor bottom automatically, and penetrating fluid is reacted from UASB
Device outflow；
The secondary Anaerobic Treatment of S4, penetrating fluid: being passed through anaerobic baffled reactor (ABR) for the penetrating fluid of step S3, leads to
It crosses baffle plate and realizes that the effect of similar two-phase separation separates penetrating fluid and sludge, infiltration is flowed out from ABR reactor；
The Air Exposure of S5, penetrating fluid: the penetrating fluid of step S4 is passed through in batch-type interval activated sludge tank (SBR) and is led to
It crosses and realizes that microorganism degrades to the organic pollutant inside penetrating fluid, precipitates organic sludge, upper layer by intermittent aerating mode
Penetrating fluid flowed out from the pond SBR；
S6, infiltration liquid disinfectant: the penetrating fluid of step S5 is passed through in sterilization pool and reaches by disinfection and meets discharge standard
Liquid discharge；
S7, Treatment of Sludge: the sludge of step S3, S4 and S5 are sent into concentration basin and pass through free settling, flocculating setting, region
Sedimentation, Compression Settlement process slough partial moisture.
Preferably, for Ca0, the penetrating fluid pH value after adjusting is the alkaline conditioner that the conditioning tank of the step S1 uses
10-12。
Preferably, the grizzly bar gap of the fine fack of the step S1 is 16-25mm.
Preferably, the carrier gas in the step S2 is air or water vapour.
Preferably, in the step S6 sterilization pool sterilization method be liquid chlorine disinfection, chlorine tablets disinfection, disinfection by chlorine dioxide,
Bleaching powder disinfection, hypochlorite disinfectant and ozonization one of which.
Compared with prior art, the beneficial effects of the present invention are: will detest inside penetrating fluid by using secondary Anaerobic Treatment
Oxygen organic is degraded, and secondary Anaerobic Treatment uses UASB reactor and ABR reactor respectively, and pole is suitable for handling highly concentrated
Waste water is spent, and sludge loss loss is smaller, is not required to set mixed stirring device, and sludge blockage problem is not present, and reduces maintenance cost,
More economically, the aerobic organic matter in penetrating fluid inside is handled by using SBR Air Exposure mode, is detested twice to realize
Oxygen processing is combined with an Aerobic Process for Treatment, and organic matter is more complete inside processing penetrating fluid；This method is also by penetrating fluid
Internal ammonia nitrogen is handled, and eutrophication situation is avoided to occur, and the penetrating fluid rear sludge generated processed passes through freedom
Sedimentation, flocculating setting, regional subsidence, Compression Settlement process come slough partial moisture can be convenient collection be used to secondary use.
Detailed description of the invention
Fig. 1 is refuse leachate process flow diagram of the invention.
Specific embodiment
Following will be combined with the drawings in the embodiments of the present invention, and technical solution in the embodiment of the present invention carries out clear, complete
Site preparation description, it is clear that described embodiments are only a part of the embodiments of the present invention, instead of all the embodiments.It is based on
Embodiment in the present invention, it is obtained by those of ordinary skill in the art without making creative efforts every other
Embodiment shall fall within the protection scope of the present invention.
As shown in Figure 1, a kind of garbage loading embeading permeates liquid processing method, comprising the following steps:
The solid impurity removal of S1, penetrating fluid: refuse landfill penetrating fluid is collected, and penetrating fluid is first passed through into fine fack and is removed
Internal solid impurity is removed, then is passed through in conditioning tank, the PH of penetrating fluid is improved；
The ammonia nitrogen removal processing of S2, penetrating fluid: the penetrating fluid of the high PH inside step S1 conditioning tank is first passed through into just precipitating, is sunk
Form sediment sludge a small amount of out, and the penetrating fluid on upper layer is passed through stripping tower, carrier gas is passed through in tower body, so that gas-liquid is contacted with each other, makes in water
The free amino molecule of dissolution passes through gas-liquid interface, shifts to gas, to complete the ammonia nitrogen removal processing of penetrating fluid；
An Anaerobic Treatment of S3, penetrating fluid: the penetrating fluid after step S2 ammonia nitrogen removal is passed through up-flow anaerobic sludge blanket
Reactor (UASB), UASB reactor bottom have a Sludge Bed, and the majority of organic pollutants in penetrating fluid is passed through here
Anaerobic fermentation is degraded to methane and carbon dioxide, because of the agitation of water flow and bubble, forms a sludge suspension layer above Sludge Bed,
UASB reactor head has equipped with three phase separator, and to gas, penetrating fluid and the mud granule after separation and fermentation, gas is certainly
The export of UASB reactor head, mud granule slide the Sludge Bed for being settled down to reactor bottom automatically, and penetrating fluid is reacted from UASB
Device outflow；
The secondary Anaerobic Treatment of S4, penetrating fluid: being passed through anaerobic baffled reactor (ABR) for the penetrating fluid of step S3, leads to
It crosses baffle plate and realizes that the effect of similar two-phase separation separates penetrating fluid and sludge, infiltration is flowed out from ABR reactor；
The Air Exposure of S5, penetrating fluid: the penetrating fluid of step S4 is passed through in batch-type interval activated sludge tank (SBR) and is led to
It crosses and realizes that microorganism degrades to the organic pollutant inside penetrating fluid, precipitates organic sludge, upper layer by intermittent aerating mode
Penetrating fluid flowed out from the pond SBR；
S6, infiltration liquid disinfectant: the penetrating fluid of step S5 is passed through in sterilization pool and reaches by disinfection and meets discharge standard
Liquid discharge；
S7, Treatment of Sludge: the sludge of step S3, S4 and S5 are sent into concentration basin and pass through free settling, flocculating setting, region
Sedimentation, Compression Settlement process slough partial moisture.
The alkaline conditioner that the conditioning tank of the step S1 uses is Ca0, and the penetrating fluid pH value after adjusting is 11, conditioning tank
It is the ammonia nitrogen removal processing of subsequent stripping tower for convenience, the grizzly bar gap of the fine fack of the step S1 is 16-25mm, thin lattice
Grid are solid-liquid separating equipment, are recycled by Mechanical Driven grizzly bar and take solid impurity out of liquid, the carrier gas in the step S2 is
Air or water vapour, the sterilization method of sterilization pool is liquid chlorine disinfection, chlorine tablets disinfection, disinfection by chlorine dioxide, drift in the step S6
Powder essence disinfection, hypochlorite disinfectant and ozonization one of which.
It is obvious to a person skilled in the art that invention is not limited to the details of the above exemplary embodiments, Er Qie
In the case where without departing substantially from spirit or essential attributes of the invention, the present invention can be realized in other specific forms.Therefore, no matter
From the point of view of which point, the present embodiments are to be considered as illustrative and not restrictive, and the scope of the present invention is by appended power
Benefit requires rather than above description limits, it is intended that all by what is fallen within the meaning and scope of the equivalent elements of the claims
Variation is included within the present invention.Any reference signs in the claims should not be construed as limiting the involved claims.
In addition, it should be understood that although this specification is described in terms of embodiments, but not each embodiment is only wrapped
Containing an independent technical solution, this description of the specification is merely for the sake of clarity, and those skilled in the art should
It considers the specification as a whole, the technical solutions in the various embodiments may also be suitably combined, forms those skilled in the art
The other embodiments being understood that.
Claims (5)
1. a kind of garbage loading embeading permeates liquid processing method, which comprises the following steps:
The solid impurity removal of S1, penetrating fluid: refuse landfill penetrating fluid is collected, and penetrating fluid is first passed through in fine fack removing
The solid impurity in portion, then be passed through in conditioning tank, improve the PH of penetrating fluid；
The ammonia nitrogen removal processing of S2, penetrating fluid: the penetrating fluid of the high PH inside step S1 conditioning tank is first passed through into just precipitating, is settled out
The penetrating fluid of a small amount of sludge, upper layer is passed through stripping tower, and carrier gas is passed through in tower body, and gas-liquid is made to contact with each other, and makes to dissolve in water
Free amino molecule pass through gas-liquid interface, to gas shift, thus complete penetrating fluid ammonia nitrogen removal processing；
An Anaerobic Treatment of S3, penetrating fluid: the penetrating fluid after step S2 ammonia nitrogen removal is passed through up-flow anaerobic sludge blanket reaction
Device (UASB), UASB reactor bottom have a Sludge Bed, and the majority of organic pollutants in penetrating fluid passes through anaerobism here
Fermentative degradation is methane and carbon dioxide, because of the agitation of water flow and bubble, forms a sludge suspension layer, UASB above Sludge Bed
Reactor head has equipped with three phase separator, and to gas, penetrating fluid and the mud granule after separation and fermentation, gas is anti-from UASB
Export at the top of device is answered, mud granule slides the Sludge Bed for being settled down to reactor bottom automatically, and penetrating fluid is flowed out from UASB reactor；
The secondary Anaerobic Treatment of S4, penetrating fluid: the penetrating fluid of step S3 is passed through anaerobic baffled reactor (ABR), passes through folding
Flowing plate realizes that the effect of similar two-phase separation separates penetrating fluid and sludge, and infiltration is flowed out from ABR reactor；
The Air Exposure of S5, penetrating fluid: the penetrating fluid of step S4 is passed through in batch-type interval activated sludge tank (SBR) by pressing
Intermittent aerating mode realizes that microorganism degrades to the organic pollutant inside penetrating fluid, precipitates organic sludge, the infiltration on upper layer
Transparent liquid is flowed out from the pond SBR；
S6, infiltration liquid disinfectant: the penetrating fluid of step S5 is passed through and reaches the liquid for meeting discharge standard in sterilization pool by disinfection
Discharge；
S7, Treatment of Sludge: the sludge of step S3, S4 and S5 are sent into concentration basin and sunk by free settling, flocculating setting, region
Drop, the process of Compression Settlement slough partial moisture.
2. a kind of garbage loading embeading according to claim 1 permeates liquid processing method, it is characterised in that: the tune of the step S1
For the alkaline conditioner that section pond uses for Ca0, the penetrating fluid pH value after adjusting is 10-12.
3. a kind of garbage loading embeading according to claim 1 permeates liquid processing method, it is characterised in that: the step S1's is thin
The grizzly bar gap of grid is 16-25mm.
4. a kind of garbage loading embeading according to claim 1 permeates liquid processing method, it is characterised in that: in the step S2
Carrier gas is air or water vapour.
5. a kind of garbage loading embeading according to claim 1 permeates liquid processing method, it is characterised in that: disappear in the step S6
The sterilization method in malicious pond is liquid chlorine disinfection, chlorine tablets disinfection, disinfection by chlorine dioxide, bleaching powder disinfection, hypochlorite disinfectant and ozone
The one of which of disinfection.
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| CN201910590539.XA CN110282828A (en) | 2019-07-02 | 2019-07-02 | A kind of garbage loading embeading infiltration liquid processing method |
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Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101041537A (en) * | 2007-04-28 | 2007-09-26 | 黄继国 | Method for treating percolation liquid of water deficiency area garbage embedding field |
| CN101302071A (en) * | 2008-06-12 | 2008-11-12 | 北京盖雅环境科技有限公司 | Method for processing palm oil waste water and use thereof |
| CN107522349A (en) * | 2016-06-22 | 2017-12-29 | 王志凤 | A kind of processing method of suitable arid area percolate from garbage filling field |
-
2019
- 2019-07-02 CN CN201910590539.XA patent/CN110282828A/en active Pending
Patent Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101041537A (en) * | 2007-04-28 | 2007-09-26 | 黄继国 | Method for treating percolation liquid of water deficiency area garbage embedding field |
| CN101302071A (en) * | 2008-06-12 | 2008-11-12 | 北京盖雅环境科技有限公司 | Method for processing palm oil waste water and use thereof |
| CN107522349A (en) * | 2016-06-22 | 2017-12-29 | 王志凤 | A kind of processing method of suitable arid area percolate from garbage filling field |
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