CN207294524U - A kind of landfill leachate film processing system - Google Patents
A kind of landfill leachate film processing system Download PDFInfo
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- CN207294524U CN207294524U CN201721216377.6U CN201721216377U CN207294524U CN 207294524 U CN207294524 U CN 207294524U CN 201721216377 U CN201721216377 U CN 201721216377U CN 207294524 U CN207294524 U CN 207294524U
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- dtnf
- processing system
- landfill leachate
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- film processing
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Abstract
The utility model discloses a kind of landfill leachate film processing system, including collecting pit, concrete sedimentation basin, anaeration in normal temperature pond, A/O MBR, sludge concentration tank, sludge filter press, DTNF/DTRO film filters, multi-effect evaporator and methane boiler, the system adds methane boiler and multi-effect evaporator on the basis of existing technology, and it instead of original rolling NF/RO film filters using DTNF/DTRO film filters, whole system is more environmentally-friendly, contamination resistance is strong, rate of recovery higher, can accomplish wastewater zero discharge.
Description
Technical field
The utility model belongs to field of garbage disposal, is to be related to a kind of landfill leachate film processing system specifically.
Background technology
Landfill leachate refers to rubbish in stacking process is filled, due to anaerobic fermentation, organic matter decompose, the leaching of precipitation
With wash away, the reason such as surface water and groundwater immersion, produce a variety of metabolites and moisture, form containing high concentration suspended matter and
The liquid of high concentration organic or inorganic component.Landfill leachate water quality characteristic is mainly:(1)The high component of organic pollution concentration is answered
It is miscellaneous;(2)Change of water quality is big;(3)Contain certain metal ion;(4)Ammonia-nitrogen content is high;(5)Biodegradability is poor(During with landfill
Between, biodegradability is more and more lower);(7)Electrical conductivity is high, salt content is high.With the increase of China's city numbers and the increasing of population
More, municipal refuse yield is in the trend risen year by year.According to statistics, the rubbish produced every year has reached 1.5 hundred million tons, it is average with
The speed in 9%/year increases, wherein undressed rubbish is 7,000,000,000 tons existing, accounts for the 8.3% of China soil sum.It is expected that in future
20 years in, the discharge capacity of solid waste by occupy 85% land, all there are serious refuse pollution to ask for national most area
Topic.The process problem of resulting landfill leachate becomes one of important topic of the world today.
The country's typical treatment process of landfill leachate is anaerobism+aerobic+UF membrane at present, its processing system such as Fig. 1 institutes
Show, there are following defect for the system:
1)Rolling NF/RO resistance tocrockings are poor
Due to the complexity of leachate quality, general bio-chemical effluent COD is in 1000mg/L or so.Rolling NF/RO antipollutions
Property it is poor, generally require influent COD to be less than 100mg/L, special resistance tocrocking rolling NF/RO water inlets also require to be less than 200mg/L.
The COD of landfill leachate is well beyond the degree that rolling NF/RO is resistant to.
2)System stability is poor
Since Landfill Leachate Pollution thing concentration is too high, cause biochemical system stability poor.And biochemical system easily by
Influenced to extraneous factor, particularly anaerobic system is to very temperature sensitive.In winter particularly northern area biochemical system water outlet
Water quality is worse, and bio-chemical effluent COD is easier to cause film often beyond 1000mg/L, even up to 2000mg/L, so high COD
Pollution.
3)On concentrated water recharge problem
Since the rate of recovery of rolling NF/RO is low, less than 60%, rolling NF causes to need the general rolling RO rate of recovery less than 70%
Want the water of recharge very big.The recharge of concentrated water can pollute the continuous enrichment of thing, particularly salinity, because whole system is to nothing
Machine salt is only to concentrate, without any removal scheme.
Utility model content
The purpose of this utility model is that to solve the above-mentioned problems and provides a kind of landfill leachate film processing system.
The utility model is achieved through the following technical solutions above-mentioned purpose:
A kind of landfill leachate film processing system, including collecting pit, concrete sedimentation basin, anaeration in normal temperature pond, A/O-MBR,
Sludge concentration tank, sludge filter press, DTNF/DTRO film filters, multi-effect evaporator and methane boiler;
Wherein described DTNF/DTRO film filters are provided with an inlet being connected with the A/O-MBR, a company
It is connected to the outlet of multi-effect evaporator concentrated water, a discharge outlet up to standard;
The multi-effect evaporator be provided with a concentrated water import being connected with the DTNF/DTRO film filters, one
Condensate drain outlet, a residue remove mouth, a steam inlet;
The methane boiler be provided with for be connected with the methane outlet in the anaeration in normal temperature pond biogas entrance, for
The steam (vapor) outlet of the steam inlet connection of the multi-effect evaporator.
Specifically, the A/O-MBR is aerobic/anaerobic membrane bioreactor.
Specifically, the filter core of the DTNF/DTRO film filters employs DTNF films and DTRO films at the same time.
As a kind of technical solution of this patent selection, the filtrate (liquid of the sludge concentration tank and the sludge filter press
Connected with the collecting pit.
Compared with prior art, the utility model has the advantages that:
The utility model adds methane boiler and multi-effect evaporator on the basis of existing system, and utilizes DTNF/
DTRO film filters instead of original rolling NF/RO film filters, and whole system is more environmentally-friendly, and contamination resistance is strong,
Rate of recovery higher, can accomplish wastewater zero discharge.
Brief description of the drawings
Fig. 1 is the structural schematic block diagram of traditional garbage percolation liquid treating system;
Fig. 2 is the structural schematic block diagram of landfill leachate film processing system described in the utility model.
Embodiment
The utility model is described in further detail below in conjunction with the accompanying drawings:
With reference to shown in Fig. 2, the utility model includes collecting pit, concrete sedimentation basin, anaeration in normal temperature pond, A/O-MBR, sludge
Concentration basin, sludge filter press, DTNF/DTRO film filters, multi-effect evaporator and methane boiler;
Wherein DTNF/DTRO film filters are provided with an inlet being connected with A/O-MBR, one and multiple-effect evaporation
The concentrated water outlet of device connection, a discharge outlet up to standard;
Multi-effect evaporator is provided with a concentrated water import being connected with DTNF/DTRO film filters, a condensed water row
Put mouth, a residue removes mouth, a steam inlet;
Methane boiler be provided with for be connected with the methane outlet in anaeration in normal temperature pond biogas entrance, be used for and multiple-effect evaporation
The steam (vapor) outlet of the steam inlet connection of device.
Wherein A/O-MBR is aerobic/anaerobic membrane bioreactor, and the filter core of DTNF/DTRO film filters uses at the same time
DTNF films and DTRO films, are dish tubular membrane, i.e., instead of the rolled film in traditional filtering device with dish tubular membrane.
As a kind of technical solution of this patent selection, the filtrate (liquid of sludge concentration tank and sludge filter press with collection
Pond connects, and filtrate returns in collecting pit and can be handled again.
The operation principle of the utility model is as follows:
The PAC added to coagulative precipitation tank refers to inorganic salt coagulant, is aluminium polychloride;PAM refers to nonionic
Type high polymer coagulant, molecular weight 1,500,000-900 ten thousand, commodity concentration is generally 8%.The effect of PAC is by it or it water
The effect completion of four aspects such as bridging is caught and is adsorbed in the compression double electric layer of solution product, electrically neutralization, winding net, can quilt
It is oxidizing to cause the particulate matter of COD to precipitate to filter out, so as to reduce COD.And PAM is high score flocculant, have
Machine high polymer coagulant has the resulting huge adsorption effect of the flco that bigger is formed between particle.
The biogas discharged from medium temperature anaerobic pond enters the burning Indoor Combustion of methane boiler, and without directly in an atmosphere
Then, more environmentally-friendly, the steam come out from methane boiler, which enters in multi-effect evaporator, to be condensed.
High efficiency filter is carried out from the liquid that A/O-MBR comes out by DTNF/DTRO film filters, it is dense in filtration apparatus
Water, which enters in multi-effect evaporator, to be evaporated, and the condensed water of multi-effect evaporator is from condensate drain outlet qualified discharge, and residue is then from residual
Slag removes mouth and removes and fill.
As depicted in figs. 1 and 2, landfill leachate film processing system described in the utility model uses high pressure resistant and anti-high pollution
The strong DTNF and DTRO films of ability substitute traditional rolled film, have the advantage that:
1)Contamination resistance is strong:Film is not easy to be blocked up by dirt, and system stability is more preferable;Influenced from Biochemical Treatment;Film makes
Use longer life expectancy.
2)Rate of recovery higher:The operating pressure higher of DTNF and DTRO, has the rate of recovery of higher, and rate of recovery highest can be done
It is less to 90-95%, the concentrated water of generation.
3)Dope accomplishes zero-emission:Dope carries out multiple-effect evaporation, and evaporation crystal is filled, accomplishes that wastewater zero discharge subtracts
Few secondary pollution.
According to the above embodiment, the utility model can be realized well.What deserves to be explained is set based on said structure
On the premise of meter, to solve same technical problem, some made on the utility model without substantive change or
Polishing, the essence of used technical solution is still as the utility model, therefore it should also be as the protection in the utility model
In the range of.
Claims (4)
1. a kind of landfill leachate film processing system, including collecting pit, concrete sedimentation basin, anaeration in normal temperature pond, A/O-MBR, dirt
Mud thickener and sludge filter press, it is characterised in that further include:
DTNF/DTRO film filters, its be provided with an inlet being connected with the A/O-MBR, one be connected with multiple-effect
The outlet of evaporator concentrated water, a discharge outlet up to standard;
Multi-effect evaporator, it is provided with a concentrated water import being connected with the DTNF/DTRO film filters, a condensed water
Floss hole, a residue remove mouth, a steam inlet;
Methane boiler, its be provided with for be connected with the methane outlet in the anaeration in normal temperature pond biogas entrance, for it is described
The steam (vapor) outlet of the steam inlet connection of multi-effect evaporator.
2. landfill leachate film processing system according to claim 1, it is characterised in that the A/O-MBR is anaerobism/good
Aerobic membrane bioreactor.
3. landfill leachate film processing system according to claim 1, it is characterised in that the DTNF/DTRO membrane filtrations
The filter core of device employs DTNF films and DTRO films at the same time.
4. landfill leachate film processing system according to claim 1, it is characterised in that the sludge concentration tank and described
The filtrate (liquid of sludge filter press is connected with the collecting pit.
Priority Applications (1)
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CN201721216377.6U CN207294524U (en) | 2017-09-21 | 2017-09-21 | A kind of landfill leachate film processing system |
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CN201721216377.6U CN207294524U (en) | 2017-09-21 | 2017-09-21 | A kind of landfill leachate film processing system |
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Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN108928980A (en) * | 2018-07-04 | 2018-12-04 | 张家港澳卓尔生物技术装备有限公司 | Percolate coprocessing system and percolate cooperative processing method |
CN109231684A (en) * | 2018-10-18 | 2019-01-18 | 中化重庆涪陵化工有限公司 | Purify the processing method and its system of ardealite storage yard penetrating fluid |
CN109836020A (en) * | 2019-04-04 | 2019-06-04 | 北京高能时代环境技术股份有限公司 | A kind of processing system and method for mature landfill leachate zero-emission |
CN111470735A (en) * | 2020-05-19 | 2020-07-31 | 厦门嘉戎技术股份有限公司 | Treatment method and system for aged leachate |
-
2017
- 2017-09-21 CN CN201721216377.6U patent/CN207294524U/en not_active Expired - Fee Related
Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN108928980A (en) * | 2018-07-04 | 2018-12-04 | 张家港澳卓尔生物技术装备有限公司 | Percolate coprocessing system and percolate cooperative processing method |
CN109231684A (en) * | 2018-10-18 | 2019-01-18 | 中化重庆涪陵化工有限公司 | Purify the processing method and its system of ardealite storage yard penetrating fluid |
CN109231684B (en) * | 2018-10-18 | 2021-09-10 | 中化重庆涪陵化工有限公司 | Treatment method and system for purifying phosphogypsum storage yard penetrating fluid |
CN109836020A (en) * | 2019-04-04 | 2019-06-04 | 北京高能时代环境技术股份有限公司 | A kind of processing system and method for mature landfill leachate zero-emission |
CN109836020B (en) * | 2019-04-04 | 2024-01-23 | 北京高能时代环境技术股份有限公司 | Treatment system and method for zero discharge of old landfill leachate |
CN111470735A (en) * | 2020-05-19 | 2020-07-31 | 厦门嘉戎技术股份有限公司 | Treatment method and system for aged leachate |
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GR01 | Patent grant | ||
GR01 | Patent grant | ||
CF01 | Termination of patent right due to non-payment of annual fee | ||
CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20180501 Termination date: 20190921 |