CN1970474A - Garbage leachate processing process and system based on membrane bioreactor-nano filtering membrane technology - Google Patents
Garbage leachate processing process and system based on membrane bioreactor-nano filtering membrane technology Download PDFInfo
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- CN1970474A CN1970474A CNA2006101574719A CN200610157471A CN1970474A CN 1970474 A CN1970474 A CN 1970474A CN A2006101574719 A CNA2006101574719 A CN A2006101574719A CN 200610157471 A CN200610157471 A CN 200610157471A CN 1970474 A CN1970474 A CN 1970474A
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- 239000012528 membrane Substances 0.000 title claims abstract description 91
- 238000000034 method Methods 0.000 title claims abstract description 45
- 238000001914 filtration Methods 0.000 title claims abstract description 30
- 239000010813 municipal solid waste Substances 0.000 title claims abstract description 22
- 238000005516 engineering process Methods 0.000 title description 10
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 109
- 239000007788 liquid Substances 0.000 claims abstract description 17
- 229910001385 heavy metal Inorganic materials 0.000 claims abstract description 15
- 238000005325 percolation Methods 0.000 claims abstract description 9
- 238000001728 nano-filtration Methods 0.000 claims description 42
- 238000006243 chemical reaction Methods 0.000 claims description 41
- 238000002203 pretreatment Methods 0.000 claims description 31
- 238000000108 ultra-filtration Methods 0.000 claims description 26
- 238000005273 aeration Methods 0.000 claims description 15
- 239000000126 substance Substances 0.000 claims description 12
- 230000001112 coagulant Effects 0.000 claims description 10
- 239000003795 chemical substances by application Substances 0.000 claims description 7
- 239000000701 coagulant Substances 0.000 claims description 7
- 238000005189 flocculation Methods 0.000 claims description 7
- 230000016615 flocculation Effects 0.000 claims description 7
- 238000001556 precipitation Methods 0.000 claims description 7
- 239000003513 alkali Substances 0.000 claims description 6
- 238000003756 stirring Methods 0.000 claims description 5
- 238000005842 biochemical reaction Methods 0.000 claims description 3
- 238000005374 membrane filtration Methods 0.000 claims description 3
- 239000002244 precipitate Substances 0.000 claims description 3
- 238000005345 coagulation Methods 0.000 claims description 2
- 230000015271 coagulation Effects 0.000 claims description 2
- 239000002245 particle Substances 0.000 abstract description 2
- 239000007769 metal material Substances 0.000 abstract 1
- 238000001223 reverse osmosis Methods 0.000 description 10
- 239000010802 sludge Substances 0.000 description 10
- 239000001301 oxygen Substances 0.000 description 8
- 229910052760 oxygen Inorganic materials 0.000 description 8
- MYMOFIZGZYHOMD-UHFFFAOYSA-N oxygen Chemical compound O=O MYMOFIZGZYHOMD-UHFFFAOYSA-N 0.000 description 8
- 238000005265 energy consumption Methods 0.000 description 6
- CVTZKFWZDBJAHE-UHFFFAOYSA-N [N].N Chemical compound [N].N CVTZKFWZDBJAHE-UHFFFAOYSA-N 0.000 description 5
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- 230000000694 effects Effects 0.000 description 3
- 238000011001 backwashing Methods 0.000 description 2
- 230000015556 catabolic process Effects 0.000 description 2
- 230000004059 degradation Effects 0.000 description 2
- 238000006731 degradation reaction Methods 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 239000002957 persistent organic pollutant Substances 0.000 description 2
- 238000011084 recovery Methods 0.000 description 2
- 239000006228 supernatant Substances 0.000 description 2
- 239000002699 waste material Substances 0.000 description 2
- 239000002351 wastewater Substances 0.000 description 2
- 230000037250 Clearance Effects 0.000 description 1
- 229920002521 Macromolecule Polymers 0.000 description 1
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- 239000003344 environmental pollutant Substances 0.000 description 1
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Classifications
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W10/00—Technologies for wastewater treatment
- Y02W10/10—Biological treatment of water, waste water, or sewage
Abstract
The invention discloses a rubbish percolation liquid disposing technique and system based on film biological reactor-nanometer filter film technique, which comprises the following steps: A. proceeding primary physicochemical disposal for rubbish percolation liquid; removing large particle and heavy metal material in the rubbish percolation liquid; forming front disposal water; B. adopting film biological reactor to do filter film disposal; generating hyperfiltration membrane water; C. filtering hyperfiltration membrane water through nanometer filter system; generating and outputting clean water. The system contains at least reacting pond, sediment pond and relative pump equipment to dispose primary physicochemical disposal, which also concludes nanometer filter system to do filtering disposal for water in the hyperfiltration membrane to output clean water.
Description
Technical field
The present invention relates to biological chemistry, relate in particular to a kind of garbage leachate treatment process and system based on the bioreactor-nano filtering membrane membrane technique.
Background technology
Percolate is the product of liquid in the landfill yard gravity flowage, be mainly derived from the interior moisture of precipitation and rubbish itself, because liquid has many factors may have influence on the character of percolate in flow process, comprise physical factor, chemical factor and biotic factor etc., so the waste water quality of percolate changes in a sizable scope.In general, its pH value is 4～9, chemical oxygen demand (COD) (COD:Chemical Oxygen Demand) 2000～62000mg/L, biochemical oxygen demand (BOD) (BOD:Biochemical Oxygen Demand) 60-45000mg/L, ammonia nitrogen (NH3-N) 1000～3000mg/l, in addition the heavy metal ion and the multiple pathogenic microorganism that also contain multiple high density, these pollutents are if directly enter the environment or the water layer that permeates the ground, and are very harmful.
Municipal wastes loading embeading percolation liquid complicated component, the organic concentration height, and its composition and character changed with " age " of garbage loading embeading, mainly show: (1) landfill initial stage biodegradability ratio of BOD/COD reaches more than 0.5, but along with the increase of landfill time, the organic concentration of the readily biodegradable in the percolate is very low, and biochemical is poor, the macromolecular substance of difficult degradation is preponderated, and causes the ratio of BOD/COD even is lower than 0.1; (2) NH3-N of high density is one of feature of percolate, causes low C/N ratio, therefore, has suitable necessity for the processing of percolate.
Chinese patent 03132053.8 disclosed a kind of garbage leachate treatment process, be at first to adopt electrolytic oxidation to handle, again through ceramic membrane filter machine filtering separation, filtered solution is through the membrane bioreactor biochemical treatment, carry out solid-liquid separation with film, water outlet is again through reverse-osmosis treated, and this kind technology weak point is: one, processing technological flow complexity, and investment is high; Two, adopt reverse osmosis method in handling, must use high-pressure pump, cause in the operational process energy consumption too high, the problem that exists electrode pad to change equally.
Summary of the invention
The object of the present invention is to provide a kind of cost garbage leachate treatment process and system based on the bioreactor-nano filtering membrane membrane technique low and easy and simple to handle, to solve cost height, technical process complicated problems in the prior art.
Garbage filter liquid processing method of the present invention adopts following steps:
A, percolate is carried out elementary materialization handle, remove macrobead and heavy metal substance in the percolate, produce pre-treatment water;
B, the pre-treatment hydromining carried out biochemical reaction with membrane bioreactor after, membrane filtration is handled again, produces water in the ultra-filtration membrane;
C, water in the ultra-filtration membrane is carried out filtration treatment, produce also output clear water by nanofiltration system.In the described steps A, described elementary materialization pack processing contains coagulation reaction, precipitation process.Described steps A comprises the steps:
A1, percolate behind the homogeneous, enter reaction tank in equalizing tank, add alkali, flocculation agent and coagulant aids in reaction tank, and stir;
A2, alkali, flocculation agent, coagulant aids and percolate produce physical reaction, generate macrobead flco and heavy metal precipitation thing, in settling tank after precipitate and separate, filtering macrobead flco and heavy metal substance, produce pre-treatment water,, the PH of pre-treatment water is pulled back to neutrality according to the water quality situation.
Also comprise in the described steps A 1 blast aeration of equalizing tank is handled.
Among the described step B, described membrane bioreactor is divided into three independently ponds, and the forebay is a pre-treatment water storage pool, and middle pond is a biological reaction tank, and after-bay is middle water storage pool.Adopt batch type aerobic/anoxic operation method, in middle pond, pre-treatment water is carried out filter membrane and handle.
Described step B comprises the steps:
During B1, input stores in the forebay in the pond in membrane bioreactor the pre-treatment water, carry out aeration and stirring first time;
B2, Zhong Chi stop aeration, and keep for some time at interval;
B3, carry out the aeration second time, simultaneously, handle by the filter membrane of membrane module, produce also water in the output ultra-filtration membrane, middle water flows into after-bay, promptly in the water storage pool.
Among the described step C, the dense water that described nanofiltration system produced returns described steps A and carries out elementary materialization processing.
Garbage percolation liquid treating system of the present invention, at least comprise percolate is carried out reaction tank, settling tank and the associated pump equipment that elementary materialization is handled, the pre-treatment water of being produced inputs to membrane bioreactor, it is characterized in that: also comprise nanofiltration system, described nanofiltration system is carried out filtration treatment to water in the ultra-filtration membrane of membrane bioreactor output, produces and the output clear water.
The membrane module of described membrane bioreactor adopts 0.1～0.2 micron ultra-filtration membrane.
The output terminal of described nanofiltration system connects the Returning pipe device to reaction tank.
Beneficial effect of the present invention is: in the present invention, taken into full account the water quality characteristics of percolate, adopted coagulating, the combination process flow process of settling tank/membrane bioreactor/nanofiltration system, by macrobead and the heavy metal substance in the coagulating sedimentation removal percolate, carry out solid-liquid separation then, pre-treatment water (being the settling tank supernatant liquor) enters membrane bioreactor, utilize the active sludge of high density to remove various organic pollutants in the waste water, ammonia nitrogen, adopt the ultra-filtration membrane membrane module to filter water in the generation simultaneously, guaranteed the membrane bioreactor effluent quality, the membrane bioreactor water outlet can directly be utilized by complete nanofiltration system; Nanofiltration system is carried out further filtration treatment to the amounts of residual contamination do in the water in the ultra-filtration membrane, produce clear water (filtrate), can be directly up to standard in order to discharging or reuse, the dense water that nanofiltration system produced then is back to reaction tank and carries out elementary materialization processing again, this " ultra-filtration membrane and nanofiltration membrane-two embrane methods " of the present invention technology, the clear water water quality high-quality of producing stable, can directly discharge or reuse.
It is a kind of new membrane separation technique that grows up on the basis of reverse osmosis that nanofiltration is handled, and under the low pressure condition, with respect to ultra-filtration technique, has higher filtration efficiency and selects perviousness.Exist nano level pore on the nanofiltration membrane, can hold back the pollution substance of most particle diameters greater than 1nm.Utilize nanofiltration system, water in the ultra-filtration membrane that membrane bioreactor produced is carried out depth type filtration to be handled, realization is held back all contaminations, nanofiltration system to the organic pollutant removal rate reach 95%, the clearance of removal of heavy metal ions rate more than 95%, NH3-N is more than 90%, chroma removal rate is greater than 90%.Make directly qualified discharge of final gained clear water, adopt the nanofiltration treatment system, required filter pressure (0.5Mpa-1.0Mpa) is less than reverse osmosis system (1.2Mpa-1.8Mpa), prior art with respect to reverse osmosis, the present invention can reach identical effect with the topping-up pump than low lift, can save energy consumption about 40%, the water rate of recovery of nanofiltration system is 60～80%.Therefore, cost of the present invention is low and easy and simple to handle.
But the complete unit nano-filtration membrane equipment of utilization independent operating of the present invention produces water to membrane bioreactor carries out the depth type filtration processing, realizes holding back all contaminations.Complete unit nano-filtration membrane equipment is by nanofiltration membrane component, instrument, pipeline, valve, high-pressure pump, controlling board cabinet and frame are formed on the spot, because the aperture of hyperfiltration membrane assembly is 0.1～0.2 micron in batch type aerobic/anoxic membrane bioreactor, less than the aperture of security personnel's strainers (5 microns), so this technology can be saved security personnel's strainer.
In elementary materialization of the present invention is handled, dosing in reaction tank (alkali, flocculation agent, coagulant aids), heavy metal ion in the dense water is precipitated out, in order to avoid the heavy metal ion of high density produces restraining effect to microorganism growth in the biological reaction tank, simultaneously, can improve the producing water ratio of integrated artistic flow process of the present invention, make the water rate of recovery of whole percolation liquid treating system can reach 80～90%.
In the present invention, membrane bioreactor adopts batch type aerobic/anoxic operation method, is similar to SBR technology, and pre-treatment water is carried out biochemical reaction, and filter membrane is handled again.Adopt intermittent aeration, water inlet and water outlet, can effectively alleviate film surface contamination material deposition, keep stable membrane flux, simultaneously capable of reducing energy consumption.With respect to SBR technology, batch type aerobic/anoxic membrane bioreactor has the advantage of SBR technology; Overcome some shortcomings of SBR technology, as activated sludge bulking, precipitation settling property difference or come-up; Adopted the sludge concentration higher than SBR technology, longer sludge retention time operation, the surplus sludge volume of generation is still less.
Specifically, the present invention has following major advantage:
(1) technical process of the present invention is simple, and by suitable design, operation can realize automatization.
(2) adopt the batch type aerobic-anoxic membrane biological reactor process treating refuse percolate of unique design can effectively remove pollutents such as organism, ammonia nitrogen.
(3) adopt nanofiltration system that batch type aerobic-anoxic Membrane Bioreactor for Wastewater Treatment water outlet is further purified, produce water water quality high-quality and stablize, can directly discharge or reuse.
(4) under identical treatment effect, owing to adopt nanofiltration system,, save one-time investment with respect to reverse osmosis system, and the energy consumption reduction, running cost descends thereupon.Specifically be compared as follows shown in the table 1:
| Economy relatively | Performance relatively | |
| Nanofiltration (NF) | NF adopts low filter pressure, and operation energy consumption reduces about 40% with respect to RO.High-pressure pump and membrane element one-time investment height. | NF and RO can remove most pollution substances in the waste liquid. |
| Reverse osmosis (RO) | RO adopts high filter pressure, and operation energy consumption height, one-time investment are also high. |
Table 1
Description of drawings
Fig. 1 is a system process structural representation of the present invention;
Fig. 2 is a typical process flow synoptic diagram of the present invention;
Fig. 3 is the concrete process flow diagram of the present invention.
Embodiment
With embodiment the present invention is described in further detail with reference to the accompanying drawings below:
According to Fig. 1, the present invention comprises equalizing tank 10, reaction tank 11, settling tank 12 and lift pump 14, the gas blower 13 that percolate is carried out elementary materialization processing successively, and biological reaction tank 2, pre-treatment water storage pool 22, middle water storage pool 23 and membrane module 21, liquid feeding pump 24, vacuum primingpump 25, mud discharging pump 26, backwashing pump 27, nanofiltration system 3 and topping-up pump 32 in the membrane bioreactor.Membrane bioreactor is divided into three independently ponds, and the forebay is a pre-treatment water storage pool 22, and middle pond is a biological reaction tank 2, and after-bay is middle water storage pool 23.
As shown in Figure 1, the pre-treatment water of being produced after the elementary materialization processing inputs in the pre-treatment water storage pool 22 of membrane bioreactor equipment regulating pondage earlier; Send into the biological reaction tank 2 of membrane bioreactor equipment again, place membrane module 21 in the biological reaction tank 2, produce water in the ultra-filtration membrane by hyperfiltration membrane assembly 21, water is sent in the middle water storage pool 23 in the ultra-filtration membrane; By topping-up pump 32 the middle water in the middle water storage pool 23 is sent into nanofiltration system 3, nanofiltration system 3 adopts complete unit nano-filtration membrane equipment by nanofiltration membrane component, instrument, pipeline, valve, high-pressure pump, controlling board cabinet and frame etc. are formed on the spot, water carries out filtration treatment in the ultra-filtration membrane that 3 pairs of membrane bioreactor equipment of this nanofiltration system produce, and produces and the output clear water.In the present invention, the membrane module 21 of the biological reaction tank 2 of membrane bioreactor equipment adopts 0.1～0.2 micron ultra-filtration membrane.
As shown in Figure 1, the dense water output terminal of nanofiltration system 3 connects Returning pipe device 30 to reaction tank 11, this Returning pipe device 30 comprises return tube 31, magnetic valve M, and magnetic valve M is installed in the return tube 31, and the dense water that nanofiltration system 3 is produced flows back to reaction tank 11 by return tube 31.
As shown in Figure 2, typical process flow of the present invention is as follows:
A, carry out elementary materialization by reaction tank 11 and 12 pairs of percolates of settling tank and handle, remove macrobead and heavy metal substance in the percolate, produce pre-treatment water.
B, to the pre-treatment hydromining with biological reaction tank 2, the pre-treatment water storage pool of membrane bioreactor
22, middle water storage pool 23 carries out the filter membrane processing, produces water in the ultra-filtration membrane.
C, carry out filtration treatment, produce also output clear water by water in 3 pairs of ultra-filtration membranes of nanofiltration system.
As shown in Figure 3, concrete technical process of the present invention is as follows:
1, percolate is collected and is flowed in the equalizing tank 10, and percolate stops in equalizing tank 10 for a long time, and carries out blast aeration in equalizing tank, makes water quality, water yield homogenizing.
2, with lift pump 14 percolate is pumped into reaction tank 11, throw in alkali, flocculation agent PAC and coagulant aids PAM, the flocculation agent of throwing in accounts for 0.1% of percolate, and coagulant aids takes a morsel, and stir and carry out coagulating, produce macrobead flco and heavy metal precipitation thing.
3, in settling tank 12 after precipitate and separate, filtering macrobead flco and heavy metal substance produce pre-treatment water, finish by above-mentioned steps 1-step 3 the elementary materialization of percolate is handled.Settling tank 12 regular spoil disposals are to sludge digestion tank, with pressure filter to sludge dewatering.
4, settling tank 12 surface loads are 0.8m
3/ m
2About h, pre-treatment water (being the settling tank supernatant liquor) exports in the pre-treatment water storage pool 22, carries out the water yield and regulates.
5, in the biological reaction tank 2 of membrane bioreactor equipment hyperfiltration membrane assembly 21 is set, carries out solid-liquid separation, hold back microorganism, improve activated sludge concentration in the membrane biological reaction pond 2; Adopt batch type aerobic/anoxic method, Controlling System aeration, water inlet and water outlet are controlled pH value under the condition about 7.2, simultaneously to the pollutent biodegrade.For example, biological reaction tank 2 adopts intermittent water inflow and water-out manners operation, cycle can be made as 1h～3h, can adopt automatic control, if when with 2h being the one-period operation, at first can establish flooding time is 5～30 minutes, treating water storage pool 22 discontinuous are carried out the aeration agitation first time during this period to biological reaction tank 2 input pre-treatment water in the past, mix the organic pollution materials in active sludge and the pre-treatment water, both are fully contacted, be beneficial to reaction.
6, then, stop aeration, and keep halted state about 30～60 minutes, this moment, dissolved oxygen descended owing to microbiological deterioration organism and ammonia nitrogen, and microorganism is in anaerobic environment in the biological reaction tank 2, and the dissolved oxygen in the pond is controlled at below the 0.5mg/L.
7, again membrane bioreactor 2 is carried out the aeration second time, simultaneously, handle, produce and export water in the ultra-filtration membrane by the filter membrane of hyperfiltration membrane assembly 21.Aeration both can replenish the required dissolved oxygen of biological degradation pollutant reaction, also can alleviate the film surface contamination, and the dissolved oxygen in the membrane bioreactor 2 is controlled at 0.5～2mg/L, and the microorganism in the pond is in aerobic environment at this moment.Like this, by step 5-step 7, alternately produce anoxic and aerobic environment in the biological reaction tank, help the carrying out of nitrification and denitrification reaction, the removal efficient of ammonia nitrogen can reach more than 85%, finishes biochemical treatment and ultrafiltration membrance filter to pre-treatment water.Can regularly start mud discharging pump 26, residual active sludge in the discharging biological reaction tank, but also discharge unit salt simultaneously.
8, water storage pool 23 during water is collected in the ultra-filtration membrane.Hyperfiltration membrane assembly 21 can start backwashing pump if any latch up phenomenon and carry out backwash.
9, by high-pressure pump water in the ultra-filtration membrane in the middle water storage pool 23 is pumped into nanofiltration system 3 to carry out advanced treatment, after the water nanofiltration is handled in 3 pairs of ultra-filtration membranes that pump into of nanofiltration system, carries out following operation:
91, produce and export clear water, directly up to standard in order to discharging or reuse.
92, the dense water of Chan Shenging returns the reaction tank 11 in the step 2, at this moment, opens magnetic valve M, and dense water flows back to reaction tank 11 by return tube 31, carries out elementary materialization again and handles.
In above-mentioned all technical process, all can by to relevant devices, device the suitable control of parts realize the automatic operation of whole process flow, as for its concrete control method, can not need to pay creative work to those skilled in the art can implement, and repeats no more herein.
In sum, although basic structure of the present invention, principle, method are specifically set forth by the foregoing description, under the prerequisite that does not break away from main idea of the present invention, according to above-described inspiration, those of ordinary skills can not need to pay creative work can implement multiple conversion/alternative form or combination, repeats no more herein.
Claims (10)
1. garbage leachate treatment process based on the bioreactor-nano filtering membrane membrane technique, it is characterized in that: it adopts following steps:
A, percolate is carried out elementary materialization handle, remove macrobead and heavy metal substance in the percolate, produce pre-treatment water;
B, the pre-treatment hydromining carried out biochemical reaction with membrane bioreactor after, membrane filtration is handled again, produces water in the ultra-filtration membrane;
C, water in the ultra-filtration membrane is carried out filtration treatment, produce also output clear water by nanofiltration system.
2. the garbage leachate treatment process based on the bioreactor-nano filtering membrane membrane technique according to claim 1 is characterized in that: in the described steps A, described elementary materialization pack processing contains coagulation reaction, precipitation process.
3. the garbage leachate treatment process based on the bioreactor-nano filtering membrane membrane technique according to claim 2 is characterized in that: described steps A comprises the steps:
A1, percolate behind the homogeneous, enter reaction tank in equalizing tank, add alkali, flocculation agent and coagulant aids in reaction tank; And stir;
A2, alkali, flocculation agent, coagulant aids and percolate produce physical reaction, generate macrobead flco and heavy metal precipitation thing, in settling tank after precipitate and separate, filtering macrobead flco and heavy metal substance, produce pre-treatment water,, the PH of pre-treatment water is pulled back to neutrality according to the water quality situation.
4. the garbage leachate treatment process based on the bioreactor-nano filtering membrane membrane technique according to claim 3 is characterized in that: also comprise in the described steps A 1 blast aeration of equalizing tank is handled.
5. the garbage leachate treatment process based on the bioreactor-nano filtering membrane membrane technique according to claim 1 is characterized in that: among the described step B, and described membrane bioreactor.
Be divided into three independently ponds, the forebay is a pre-treatment water storage pool, and middle pond is a biological reaction tank, and after-bay is middle water storage pool, adopts batch type aerobic/anoxic operation method, in middle pond pre-treatment water is carried out filter membrane and handles.
6. the garbage leachate treatment process based on the bioreactor-nano filtering membrane membrane technique according to claim 5 is characterized in that: described step B comprises the steps:
During B1, input stores in the forebay in the pond in membrane bioreactor the pre-treatment water, carry out aeration and stirring first time;
B2, Zhong Chi stop aeration, and keep for some time at interval;
B3, carry out the aeration second time, simultaneously, handle by the filter membrane of membrane module, produce also water in the output ultra-filtration membrane, middle water flows into after-bay, promptly in the water storage pool.
7. according to any described garbage leachate treatment process among the claim 1-6 based on the bioreactor-nano filtering membrane membrane technique, it is characterized in that: among the described step C, the dense water that described nanofiltration system produced returns described steps A and carries out elementary materialization processing.
8. garbage percolation liquid treating system based on the bioreactor-nano filtering membrane membrane technique, at least comprise percolate is carried out reaction tank, settling tank and the associated pump equipment that elementary materialization is handled, the pre-treatment water of being produced inputs to membrane bioreactor, it is characterized in that: also comprise nanofiltration system, described nanofiltration system is carried out filtration treatment to water in the ultra-filtration membrane of membrane bioreactor output, produces and the output clear water.
9. the garbage percolation liquid treating system based on the bioreactor-nano filtering membrane membrane technique according to claim 8 is characterized in that: the membrane module of described membrane bioreactor adopts 0.1～0.2 micron ultra-filtration membrane.
10. it is characterized in that according to Claim 8 or 9 described garbage percolation liquid treating systems based on the bioreactor-nano filtering membrane membrane technique: the output terminal of described nanofiltration system connects the Returning pipe device to reaction tank.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
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| CNB2006101574719A CN100532299C (en) | 2006-12-11 | 2006-12-11 | Garbage leachate processing process and system based on membrane bioreactor-nano filtering membrane technology |
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| CNB2006101574719A CN100532299C (en) | 2006-12-11 | 2006-12-11 | Garbage leachate processing process and system based on membrane bioreactor-nano filtering membrane technology |
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| CN1970474A true CN1970474A (en) | 2007-05-30 |
| CN100532299C CN100532299C (en) | 2009-08-26 |
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Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101786716A (en) * | 2010-02-10 | 2010-07-28 | 德威华泰（北京）科技有限公司 | High-concentration difficult-degradation organic sewage treating system |
| CN101928094B (en) * | 2009-10-12 | 2012-07-04 | 杭州深瑞水务有限公司 | Technology for treating garbage leachate |
| CN102730825A (en) * | 2012-06-20 | 2012-10-17 | 太平洋水处理工程有限公司 | Modified CAST equipment and technology employing submerged hollow fiber ultrafiltration membranes |
| CN103130378A (en) * | 2011-11-24 | 2013-06-05 | 马志文 | System for treating household garbage leachate |
| CN104370344A (en) * | 2014-11-27 | 2015-02-25 | 上海世渊环保科技有限公司 | Advanced treatment method and advanced treatment system for landfill leachate |
| CN105712586A (en) * | 2016-04-28 | 2016-06-29 | 房沙沙 | Refuse landfill site leachate treatment system |
| CN105884128A (en) * | 2016-04-09 | 2016-08-24 | 深圳市赛威赢环境技术工程有限公司 | Nickel-containing wastewater treating system and method |
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| CN105884128A (en) * | 2016-04-09 | 2016-08-24 | 深圳市赛威赢环境技术工程有限公司 | Nickel-containing wastewater treating system and method |
| CN105712586A (en) * | 2016-04-28 | 2016-06-29 | 房沙沙 | Refuse landfill site leachate treatment system |
| CN109110918A (en) * | 2018-09-18 | 2019-01-01 | 戚汝常 | A kind of novel SBR-MBR sewage disposal system and technique |
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