CN109574372A - A kind of processing method of consumer waste infiltration liquid - Google Patents
A kind of processing method of consumer waste infiltration liquid Download PDFInfo
- Publication number
- CN109574372A CN109574372A CN201710909862.XA CN201710909862A CN109574372A CN 109574372 A CN109574372 A CN 109574372A CN 201710909862 A CN201710909862 A CN 201710909862A CN 109574372 A CN109574372 A CN 109574372A
- Authority
- CN
- China
- Prior art keywords
- processing
- uasb
- consumer waste
- infiltration liquid
- water outlet
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
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- 238000003672 processing method Methods 0.000 title claims abstract description 15
- 238000001764 infiltration Methods 0.000 title claims abstract description 14
- 239000007788 liquid Substances 0.000 title claims abstract description 12
- 239000002699 waste material Substances 0.000 title claims abstract description 12
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances data:image/svg+xml;base64,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 data:image/svg+xml;base64,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 O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 26
- 230000001112 coagulant Effects 0.000 claims abstract description 15
- 238000009280 upflow anaerobic sludge blanket technology Methods 0.000 claims abstract description 14
- 239000000149 chemical water pollutant Substances 0.000 claims abstract description 11
- 238000000034 method Methods 0.000 claims abstract description 9
- 238000001556 precipitation Methods 0.000 claims abstract description 9
- 239000003344 environmental pollutant Substances 0.000 claims abstract description 7
- 231100000719 pollutant Toxicity 0.000 claims abstract description 7
- 239000012466 permeate Substances 0.000 claims abstract description 6
- 238000004062 sedimentation Methods 0.000 claims abstract description 6
- 239000000126 substance Substances 0.000 claims abstract description 4
- 238000011068 load Methods 0.000 claims abstract description 3
- 238000001223 reverse osmosis Methods 0.000 claims description 3
- RBTARNINKXHZNM-UHFFFAOYSA-K Iron(III) chloride Chemical group 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Cl[Fe](Cl)Cl RBTARNINKXHZNM-UHFFFAOYSA-K 0.000 claims description 2
- 239000004411 aluminium Substances 0.000 claims description 2
- 229910052782 aluminium Inorganic materials 0.000 claims description 2
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminum Chemical compound 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- 238000006731 degradation reaction Methods 0.000 description 5
- CVTZKFWZDBJAHE-UHFFFAOYSA-N [N].N Chemical compound 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[N].N CVTZKFWZDBJAHE-UHFFFAOYSA-N 0.000 description 4
- 241000894006 Bacteria Species 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 239000012528 membrane Substances 0.000 description 2
- OAICVXFJPJFONN-UHFFFAOYSA-N phosphorus Chemical compound 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[P] OAICVXFJPJFONN-UHFFFAOYSA-N 0.000 description 2
- 229910052698 phosphorus Inorganic materials 0.000 description 2
- 239000011574 phosphorus Substances 0.000 description 2
- 238000010992 reflux Methods 0.000 description 2
- 238000000926 separation method Methods 0.000 description 2
- 239000010802 sludge Substances 0.000 description 2
- 239000002689 soil Substances 0.000 description 2
- 239000006228 supernatant Substances 0.000 description 2
- 241000233866 Fungi Species 0.000 description 1
- 230000003851 biochemical process Effects 0.000 description 1
- 238000001311 chemical methods and process Methods 0.000 description 1
- 238000005345 coagulation Methods 0.000 description 1
- 230000015271 coagulation Effects 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 238000011049 filling Methods 0.000 description 1
- 239000000706 filtrate Substances 0.000 description 1
- 239000003673 groundwater Substances 0.000 description 1
- 239000004615 ingredient Substances 0.000 description 1
- 239000002054 inoculum Substances 0.000 description 1
- 230000014759 maintenance of location Effects 0.000 description 1
- 244000005700 microbiome Species 0.000 description 1
- 238000006396 nitration reaction Methods 0.000 description 1
- 238000005086 pumping Methods 0.000 description 1
- 239000002352 surface water Substances 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F9/00—Multistage treatment of water, waste water, or sewage
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/001—Processes for the treatment of water whereby the filtration technique is of importance
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/44—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
- C02F1/5236—Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities using inorganic agents
- C02F1/5245—Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities using inorganic agents using basic salts, e.g. of aluminium and iron
-
- 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
- C02F1/54—Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities using organic material
- C02F1/56—Macromolecular compounds
-
- 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
- C02F2101/00—Nature of the contaminant
- C02F2101/10—Inorganic compounds
- C02F2101/20—Heavy metals or heavy metal compounds
-
- 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
-
- 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
- C02F3/2846—Anaerobic digestion processes using upflow anaerobic sludge blanket [UASB] reactors
Abstract
The invention discloses a kind of processing methods of consumer waste infiltration liquid, including (1) grid: intercepting from reservoir by mechanical grille, the suspended matter in water is effectively reduced, lighten the load for subsequent handling processing.(2) coagulating sedimentation: grid water outlet is promoted to coagulative precipitation tank with elevator pump, by dosing coagulating sedimentation, removes removing heavy metals, SS and partial organic substances pollutant.(3) UASB: coagulative precipitation tank water outlet pump obtains after being promoted to UASB processing.(4) MBR technique: enter in MBR processor through UASB water outlet and be further processed to obtain first time permeate；(5) DTRO: film is concentrated by dish tubular type in first time permeate, is discharged.The processing method of consumer waste infiltration liquid of the invention has easy to operate, obvious processing effect, and saving power and preventing pollution dye is practical, can efficiently remove organic matter and heavy metal in landfill leachate, landfill leachate treatment is made to reach the target of " zero-emission ".
Description
Technical field
The invention belongs to environmental technology fields, and in particular to a kind of processing method of consumer waste infiltration liquid.
Background technique
With the development of city process, there is a sharp increase in output for municipal refuse caused by population collection.Place both economical at present
Reason method is sanitary landfills to be carried out to it, and problem maximum brought by filling is the generation of landfill leachate, and ingredient is multiple
It is miscellaneous, organic concentration is high, water quality and quantity changes greatly.Although this effluent part amount is little, pollution level is quite high, can be tight
Lead to water body, soil, atmosphere pollution again, threat is brought to human health.
Landfill leachate is different from municipal sewage, in general, the COD concentration of landfill leachate be sanitary sewage 10 ~
100 times.And pollutant kind is complicated, water, the change of water quality of different times are larger, and percolate is the most important pollution of underground water
Quite serious pollution is caused to environment by contacting with soil, ground or surface water in source.Current domestic and international landfill leachate
Processing method mainly have biochemical process, physical-chemical process, recharge method etc..Although biochemical processing method operating cost is relatively
It is low, but water outlet be difficult it is up to standard.Leachate recirculation is percolate processing method the most economic, but the percolate of this method processing cannot
Direct emission.With the development of technology, membrane separation technique has been widely used in sanitary sewage, in municipal sewage treatment, mesh
Before be also applicable in the processing of landfill leachate.Membrane separation technique can efficiently retain pollutant, and application is simple.By several
The connected applications of kind processing method, can reliably handle landfill leachate, make up to discharge standard.
Summary of the invention
The purpose of the present invention is to provide a kind of easy to operate, economical and efficient, environmental protection rubbish without secondary pollution, practical
The sewage water treatment method of rubbish percolate.
The processing method of consumer waste infiltration liquid of the invention, including following processing step:
(1) grid: intercepting by mechanical grille from reservoir, the suspended matter in water be effectively reduced, and subtracts for subsequent handling processing
Light load；
(2) coagulating sedimentation: grid water outlet is promoted to coagulative precipitation tank with elevator pump, by dosing coagulating sedimentation, a removal huge sum of money
Category, SS and partial organic substances pollutant；
(3) UASB: coagulative precipitation tank water outlet pump obtains after being promoted to UASB processing；
(4) MBR technique: enter in MBR processor through UASB water outlet, by the reaction of microorganism fungus kind and the retention of film, into one
Step handles to obtain first time permeate；
(5) DTRO: first time permeate is entered into disc tube reverse osmosis (dt-ro) film column, obtains clear water and concentrate.Clear water can be direct
For discharging or carrying out equipment backwash, concentrate reflux reenters coagulative precipitation tank and carries out circular treatment.
The processing method of consumer waste infiltration liquid of the invention, the COD of percolate are 2000 mg/L-80000 mg/L, pH
Between 4 ~ 9.
Flocculant selected by the present invention is ferric trichloride, aluminium polychloride, polyacrylamide.
It is 200mg/L or less the present invention claims UASB influent quality SS concentration.
The processing method of consumer waste infiltration liquid of the invention first removes a large amount of SS, highly concentrated contained in landfill leachate
Heavy metal, ammonia nitrogen, COD of degree etc..Then by biochemistry by 80% or more ammonia nitrogen removal in pollutant, finally pass through the infiltration of film
Thoroughly, pollutant heavy metal removing rate is made to reach 95% or more, concentrate is back in UASB that the reaction was continued, is finally reached rubbish infiltration
The target of filtrate " zero-emission ".
Specific embodiment
The interception that 100 tons of landfill leachates are first passed through to grid puts into flocculant into coagulative precipitation tank, and reaction 1 is small
When, supernatant and sludge are obtained, by supernatant pumping into UASB reactor, sludge reflux to collecting pit.It is heavy by coagulation
It forms sediment and further removes SS, 50% or more total phosphorus and partial organic substances.It can make sewage by 24 hours UASB reactor reactions
COD reduces by 50%, is extracted into MBR reactor by the water of anaerobic jar output by water pump, added in MBR reactor ammonia nitrogen degradation bacterium,
COD degradation bacterium nitrified, anti-nitration reaction, makes ammonia nitrogen degradation 80 ~ 90% by the reaction of biological inoculum, and COD degradation 80 ~
90%, total phosphorus degradation 90%.MBR water outlet enters disc tube reverse osmosis (dt-ro) filter apparatus, obtains clear water and concentrate, concentrate is led to
Piping is back in coagulative precipitation tank.By process above process, sewage is made to be finally reached discharge standard.
Claims (4)
1. a kind of processing method of consumer waste infiltration liquid, which is characterized in that including following processing step:
(1) grid: intercepting by mechanical grille from reservoir, the suspended matter in water be effectively reduced, and subtracts for subsequent handling processing
Light load；
(2) coagulating sedimentation: grid water outlet is promoted to coagulative precipitation tank with elevator pump, by dosing coagulating sedimentation, a removal huge sum of money
Category, SS and partial organic substances pollutant；
(3) UASB: coagulative precipitation tank water outlet pump obtains after being promoted to UASB processing；
(4) MBR technique: enter in MBR processor through UASB water outlet and be further processed to obtain first time permeate；
(5) it DTRO: by first time permeate by disc tube reverse osmosis (dt-ro) film, is discharged.
2. the processing method of consumer waste infiltration liquid as described in claim 1, which is characterized in that the landfill leachate
CODCr is 2000mg/L ~ 80000mg/L, and pH is between 4 ~ 9.
3. the processing method of consumer waste infiltration liquid as described in claim 1, which is characterized in that flocculation described in step (2)
Agent is ferric trichloride, aluminium polychloride, polyacrylamide.
4. the processing method of consumer waste infiltration liquid as described in claim 1, which is characterized in that UASB described in step (3)
It is 200mg/L or less that water inlet requirement, which need to reach SS concentration,.
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