CN1456521A - Process and apparatus for urban refuse cite penetrating liquid by three stage plus one process - Google Patents
Process and apparatus for urban refuse cite penetrating liquid by three stage plus one process Download PDFInfo
- Publication number
- CN1456521A CN1456521A CN 03121161 CN03121161A CN1456521A CN 1456521 A CN1456521 A CN 1456521A CN 03121161 CN03121161 CN 03121161 CN 03121161 A CN03121161 A CN 03121161A CN 1456521 A CN1456521 A CN 1456521A
- Authority
- CN
- China
- Prior art keywords
- section
- percolate
- advanced treatment
- handles
- stage process
- 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.)
- Granted
Links
Landscapes
- Physical Water Treatments (AREA)
- Separation Using Semi-Permeable Membranes (AREA)
- Treatment Of Water By Oxidation Or Reduction (AREA)
Abstract
A process and apparatus for treating the seeping liquid of garbage burying field is disclosed, which features that 4 treating segments are included. The first segment is composite anaerobic reaction segment for anaerobic fermenting, recovering marsh gas and greatly degradating organic substance. The second segment is blowing-denitrifying segment for removing suspended substance and blowing out ammoniacal nitrogen. The third segment is A/O-A/O biochemical one for removing organic substance and ammmoniacal nitrogen. The last one is nano-filter further treating segment for further removing residual organic substance and colibacillus. Its advantages are high effect and low cost.
Description
Technical field
The present invention relates to a kind of Processes and apparatus of handling percolation liquid of city life garbage landfill.
Background technology
Along with expanding economy, the raising of living standards of the people, the domestic waste amount is developing with the annual growth of 6%-10%, the many exposed stackings in the suburb of municipal wastes, cause soil, water body, atmospheric severe contamination and transmission of disease, to become the social concern that influences human survival.Domestic waste landfill disposal technology is low with reduced investment, working cost, and obtains widespread use.But, in the garbage loading embeading process, also brought percolate secondary pollution problem.Percolate has the basicity height, the ammonia nitrogen concentration height, and the high and high outstanding feature of organic cod concentration of ph value belongs to very unmanageable high concentrated organic wastewater.From domestic garbage loading embeading situation, the generation of percolate is subjected to many factor affecting at present, and the water yield changes greatly, the water-quality constituents complexity, and its biodegradability becomes worse and worse along with the landfill yard field increases age, brings great difficulty for the operational management of treatment facility.Be qualified discharge, if adopt external complicated technology, it is very expensive to handle working cost, does not meet China's actual conditions.Existing main methods and equipment have following several:
1, anaerobic biological treatment: the processing that contains the percolate of high density waste for landfill yard in early days is fit to adopt anaerobic reactor to carry out pre-treatment.Anaerobic reactor is when handling the high density percolate, and tool has great advantage, consume energy low, take up an area of less.But the water outlet Pollutant levels are higher, and directly therefore qualified discharge must unite use with other treatment process.
2, aerobe is handled: aerobic treatment technology is CDDcr, the BOD in the water of place to go effectively
5, ammonia nitrogen and heavy metal thing etc.Because the low floor space of treatment process load is big, has certain limitation in the application.But for the processing of handling through the percolate of anaerobic treatment, can give full play to long characteristics of its residence time, tool has great advantage.
3, physico-chemical process: physico-chemical process processing costs height, especially directly handle percolate stoste, the processing costs costliness has limited the development and the application of these methods.
4, recharging technique: recharging technique technology is with leachate collection, makes it to be back to the technology of garbage loading embeading by sprinkling irrigation, can quicken the decomposition of component of refuse, can also realize the percolate minimizing by Evaporation.Recharging technique exists many technical problems not to be resolved at present. (1) blockage problem, because suspended solids content is higher in the percolate, the microbial reproduction amount is bigger simultaneously, is easy to make landfill layer space to stop up; (2) the acid accumulation problem appears in anaerobic digestion in the waste layer, reduces the further biochemical speed of organism; (3) low to ammonia nitrogen removal efficient; (4) foul smell that distributes during surface sprinkling causes secondary pollution to environment.Because the existence of these problems makes recharging technique have significant limitation in the sanitary filling field percolate is handled.To sum up, be badly in need of seeking a kind of leachate treatment technology of economical rationality, to reach three unifications of society, economy, environmental benefit.
Technology contents
The purpose of this invention is to provide a kind of " three-stage process+1 " and handle the Processes and apparatus of percolation liquid of city life garbage landfill, solve percolation liquid of city life garbage landfill secondary pollution problem of environment.
The present invention " three-stage process+1 " handles the technical scheme of percolation liquid of city life garbage landfill technology: it is characterized in that: add nanofiltration advanced treatment section by first section, second section, the 3rd section and be linked in sequence and form,
First section is the composite anaerobic conversion zone, and percolate enters hybrid anaerobic reactor, carries out anaerobically fermenting, reclaims biogas energy and degradation of organic substances significantly;
Second section is stripping denitrogenation section, and the percolate after the anaerobism passes through stripping tower stripping ammonia nitrogen again through the suspended substance of Induced-draft air float machine removal percolate;
The 3rd section is the biochemical section of A/O-A/O, is continued to remove the organism and the ammonia nitrogen of percolate by the A/O biological contact oxidation pond;
"+1 " is nanofiltration advanced treatment section, carries out advanced treatment by the nanofiltration membrane treatment device, and bio-refractory organism and coliform are further removed.
A kind of " three-stage process+1 " handles the equipment of percolation liquid of city life garbage landfill, it is characterized in that: be linked in sequence by hybrid anaerobic reactor, Induced-draft air float machine, stripping tower, A/O contact-oxidation pool and nanofiltration advanced treatment apparatus.
Connect equalizing tank and heat exchanger before the above-mentioned hybrid anaerobic reactor.
Above-mentioned A/O biological contact oxidation pond bottom is communicated with gas blower, and the liquid outlet of A/O biological contact oxidation pond is connected with second pond.
Connect the nanofiltration advanced treatment apparatus behind the above-mentioned second pond.
Beneficial effect: " three-stage process+1 " is the reasonable combination of utilizing biochemistry, materialization principle, adopting several treatment process and device; Economical, effectively handle a kind of novel process technology of percolation liquid of city life garbage landfill, be suitable for the condition of water quality of landfill percolate: pH5.8-8.0; COD 6000-20000mg/L; SS＜30000mg/L; Ammonia nitrogen＜3000mg/L.Leachate quality alters a great deal in time, organic concentration height in the summer percolate, CODcr/NH
4-N is than height, BOD
5/ CODcr height, basicity is relatively low, and pH is also lower, and biodegradability is good, and is better for biochemical treatment water quality.And in the winter time, organic concentration reduces, percolate CODcr/NH
4-N is low, BOD
5/ CODcr is low, and ammonia nitrogen concentration raises, and pH raises, and the water quality biodegradability is relatively poor, and for biochemical treatment, water quality is abominable.
There are hybrid anaerobic reactor unit, air supporting and stripping unit, A/O-A/O catalytic oxidation unit in main technique of the present invention unit, is called three sections, and first three section belongs to percolate two stage biological treating processes, after add one section and carry out advanced treatment for the nanofiltration membrane treatment device.When effluent quality reaches first discharge standard, compared with prior art, following characteristics are arranged:
1, " three-stage process+1 " Technology that adopts anaerobism, stripping, A/O, nanofiltration technique to form can be handled the pollutent in the percolate effectively, and treat effluent reaches the GB first discharge standard.
2, " three-stage process+1 " handles percolate, and wherein " three-stage process " born CODcr and the 95% above ammonia nitrogen removal frank more than 85%, and nanofiltration mainly is to remove the organism that is difficult to biochemical degradation, guarantees that water outlet CODcr is up to standard.
3, A/O catalytic oxidation, filling carrier is set increases biomass, improves CODcr and handles load, makes A/O oxidation pond organic loading reach 0.2-0.3kgCODcr/m
3.d, has 83.9% COOcr clearance.The aeration denitrogenation combines with biological denitrificaion and makes it have 98% deoxidation effect in the A/O pond, and A/O bears in the pond concentration of ammonia nitrogen can be up to 300-700mg/l.
4, the main technical details of " three-stage process+1 " Technology has been proposed: ph value, ammonia nitrogen, basicity, temperature, solved the problems of emerged in operation, in time the adjusting process parameter guarantees that treatment effect is reliable and stable.
5, hybrid anaerobic reactor is handled percolate, and the biogas rate is 0.35-0.56m
3/ kg.CODcr reclaims this part biogas, is used for the intensification of anaerobism workshop section, and save energy is taken, and reduces working cost.
6, rationally utilize the high basicity of percolate, high ammonia nitrogen, high pH value characteristic, under adjust pH situation not, can carry out the stripping ammonia nitrogen smoothly, deoxidation efficient reaches 53%-71%, guarantees that water outlet reaches the first discharge standard of GB16889-1997 " consumer waste filling and embedding pollution control criterion " regulation.Save medicament expense, working cost reduces, and ton water treatment expense is about 11.49 yuan/t. percolate, and it is most economical comparing with processing costs in the percolate both domestic and external field, is applicable to the processing of consumer waste landfill percolate.
Description of drawings
Fig. 1 is that " three-stage process+1 " handles percolation liquid of city life garbage landfill technical process and equipment connection diagram.
Among the figure: 1-equalizing tank, 2-heat exchanger, 3-anaerobic reactor, 4-Induced-draft air float machine, 5-stripping tower, 6-A/O contact-oxidation pool, 7-gas blower, 8-second pond, 9-nanofiltration advanced treatment apparatus.
Embodiment
" three-stage process+1 " handles percolation liquid of city life garbage landfill technology, adding nanofiltration advanced treatment section by first section, second section, the 3rd section is linked in sequence and forms, first section is the composite anaerobic conversion zone, percolate enters hybrid anaerobic reactor 3, carry out anaerobically fermenting, reclaim biogas energy and degradation of organic substances significantly; Second section is stripping denitrogenation section, and the percolate after the anaerobism passes through stripping tower 5 stripping ammonia nitrogens again through the suspended substance of Induced-draft air float machine 4 removal percolates; The 3rd section is the biochemical section of A/O-A/O, is continued to remove the organism and the ammonia nitrogen of percolate by A/O biological contact oxidation pond 6; "+1 " is nanofiltration advanced treatment section, carries out advanced treatment by nanofiltration advanced treatment apparatus 9, and bio-refractory organism and coliform are further removed.Guarantee that water outlet reaches the first discharge standard requirement of GB16889-1997 " consumer waste filling and embedding pollution control criterion " regulation.
" three-stage process+1 " handles the equipment of percolation liquid of city life garbage landfill, is linked in sequence by hybrid anaerobic reactor 3, Induced-draft air float machine 4, stripping tower 5, A/O contact-oxidation pool 6 and nanofiltration advanced treatment apparatus 9.Connect equalizing tank 1 and heat exchanger 2 before the above-mentioned hybrid anaerobic reactor.Above-mentioned A/O biological contact oxidation can adopt the secondary anaerobic series operation, the A/O contact-oxidation pool can change the aeration rate size, A/O biological contact oxidation pond bottom is communicated with gas blower 7, and the liquid outlet of A/O biological contact oxidation pond is connected with second pond 8, connects nanofiltration advanced treatment apparatus 9 behind the second pond.
" three-stage process+1 " technical data:
1 leachate quality condition
pH 5.8-8.0
COD
cr 6000-20000mg/L
SS ＜30000mg/L
Ammonia nitrogen＜3000mg/L
2 hybrid anaerobic reactors
Controlled temperature 33+5 ℃
COD
CrLoad 4-8kgCOD
Cr/ m
3.d
COD
CrClearance 68-90%
SS clearance＞70%
Ammonia nitrogen removal frank 8-12%
Biogas generation 0.38-0.56m
3/ kgCOD
Cr
3 Induced-draft air float machines
Air supporting time 45min
Dosage PAC 0-300ppm
PAM?0-10ppm
SS clearance 56-90%
COD
CrClearance 8-30%
4 stripping towers
Filler draws two rings, Pall ring or cascade ring D=50mm
Packed height 5.5m-6.0m
The compound 4-6m of water distribution
3/ m
2.h
Temperature＞15 ℃
Water temperature＞15 ℃
pH 8.5-9.5
Water: gas 1: 2000
Ammonia nitrogen removal frank 53-71%
The 5A/O-A/O contact-oxidation pool
Water temperature 16-28 ℃
pH ＜8.0
COD
cr ＜2000mg/L
Ammonia nitrogen＜400mg/L
COD
CrLoad 0.18-0.25kgCOD
Cr/ m
3.d
6 nanofiltration advanced treatment systems
Operating pressure＜0.7MPa
Water temperature＞10
Water inlet COD
Cr＜800mg/L water outlet＜100mg/L
Influent ammonia nitrogen＜30mg/L water outlet＜15mg/L
Claims (5)
1, a kind of " three-stage process+1 " handles the technology of percolation liquid of city life garbage landfill, it is characterized in that: add nanofiltration advanced treatment section by first section, second section, the 3rd section and be linked in sequence and form,
First section is the composite anaerobic conversion zone, and percolate enters hybrid anaerobic reactor, carries out anaerobically fermenting, reclaims biogas energy and degradation of organic substances significantly;
Second section is stripping denitrogenation section, and the percolate after the anaerobism passes through stripping tower stripping ammonia nitrogen again through the suspended substance of Induced-draft air float machine removal percolate;
The 3rd section is the biochemical section of A/O-A/O, is continued to remove the organism and the ammonia nitrogen of percolate by the A/O biological contact oxidation pond;
"+1 " is nanofiltration advanced treatment section, carries out advanced treatment by the nanofiltration advanced treatment apparatus, and bio-refractory organism and coliform are further removed.
2, a kind of " three-stage process+1 " handles the equipment of percolation liquid of city life garbage landfill, it is characterized in that: be linked in sequence by hybrid anaerobic reactor, Induced-draft air float machine, stripping tower, A/O contact-oxidation pool and nanofiltration advanced treatment apparatus.
3, " three-stage process+1 " according to claim 2 handles the equipment of percolation liquid of city life garbage landfill, it is characterized in that: connect equalizing tank and heat exchanger before the described hybrid anaerobic reactor.
4, " three-stage process+1 " according to claim 2 handles the equipment of percolation liquid of city life garbage landfill, it is characterized in that: described A/O biological contact oxidation pond bottom is communicated with gas blower, and the liquid outlet of A/O biological contact oxidation pond is connected with second pond.
5, " three-stage process+1 " according to claim 4 handles the equipment of percolation liquid of city life garbage landfill, it is characterized in that: connect the nanofiltration advanced treatment apparatus behind the described second pond.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB031211615A CN1176034C (en) | 2003-03-28 | 2003-03-28 | Process and apparatus for urban refuse cite penetrating liquid by three stage plus one process |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB031211615A CN1176034C (en) | 2003-03-28 | 2003-03-28 | Process and apparatus for urban refuse cite penetrating liquid by three stage plus one process |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN1456521A true CN1456521A (en) | 2003-11-19 |
| CN1176034C CN1176034C (en) | 2004-11-17 |
Family
ID=29411600
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CNB031211615A Expired - Fee Related CN1176034C (en) | 2003-03-28 | 2003-03-28 | Process and apparatus for urban refuse cite penetrating liquid by three stage plus one process |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN1176034C (en) |
Cited By (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1329318C (en) * | 2005-09-14 | 2007-08-01 | 北京天地人环保科技有限公司 | Method for disposing refuse leachate of domestic refuse landfill |
| CN1331780C (en) * | 2004-11-04 | 2007-08-15 | 中国科学院生态环境研究中心 | Integrative bioreactor for treating refuse leachate |
| CN100336749C (en) * | 2004-09-14 | 2007-09-12 | 北京大学 | Garbage percolation liquid treating system and method |
| CN100398470C (en) * | 2006-03-17 | 2008-07-02 | 深圳市百斯特环保工程有限公司 | Infiltration method for treating garbage |
| CN100406399C (en) * | 2005-08-01 | 2008-07-30 | 陈昆柏 | Method and system for harnessing consumer waste landfill percolate |
| CN100478289C (en) * | 2007-07-13 | 2009-04-15 | 北京大学 | Method for treating medium and terminal garbage percolate |
| CN102295387A (en) * | 2011-07-27 | 2011-12-28 | 上海复旦水务工程技术有限公司 | Device and method for processing high-density landfill leachate |
| CN111847809A (en) * | 2019-12-30 | 2020-10-30 | 重庆大学 | Kitchen waste fermentation wastewater treatment device and method |
| CN111847796A (en) * | 2020-07-31 | 2020-10-30 | 中节能工程技术研究院有限公司 | System and method for treating leachate of waste incineration plant |
| CN116332396A (en) * | 2023-02-23 | 2023-06-27 | 上海环境卫生工程设计院有限公司 | Landfill leachate recycling treatment method |
-
2003
- 2003-03-28 CN CNB031211615A patent/CN1176034C/en not_active Expired - Fee Related
Cited By (12)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN100336749C (en) * | 2004-09-14 | 2007-09-12 | 北京大学 | Garbage percolation liquid treating system and method |
| CN1331780C (en) * | 2004-11-04 | 2007-08-15 | 中国科学院生态环境研究中心 | Integrative bioreactor for treating refuse leachate |
| CN100406399C (en) * | 2005-08-01 | 2008-07-30 | 陈昆柏 | Method and system for harnessing consumer waste landfill percolate |
| CN1329318C (en) * | 2005-09-14 | 2007-08-01 | 北京天地人环保科技有限公司 | Method for disposing refuse leachate of domestic refuse landfill |
| CN100398470C (en) * | 2006-03-17 | 2008-07-02 | 深圳市百斯特环保工程有限公司 | Infiltration method for treating garbage |
| CN100478289C (en) * | 2007-07-13 | 2009-04-15 | 北京大学 | Method for treating medium and terminal garbage percolate |
| CN102295387A (en) * | 2011-07-27 | 2011-12-28 | 上海复旦水务工程技术有限公司 | Device and method for processing high-density landfill leachate |
| CN111847809A (en) * | 2019-12-30 | 2020-10-30 | 重庆大学 | Kitchen waste fermentation wastewater treatment device and method |
| CN111847796A (en) * | 2020-07-31 | 2020-10-30 | 中节能工程技术研究院有限公司 | System and method for treating leachate of waste incineration plant |
| CN111847796B (en) * | 2020-07-31 | 2024-04-09 | 中节能工程技术研究院有限公司 | Leachate treatment system and method for garbage incineration plant |
| CN116332396A (en) * | 2023-02-23 | 2023-06-27 | 上海环境卫生工程设计院有限公司 | Landfill leachate recycling treatment method |
| CN116332396B (en) * | 2023-02-23 | 2024-08-20 | 上海环境卫生工程设计院有限公司 | Landfill leachate recycling treatment method |
Also Published As
| Publication number | Publication date |
|---|---|
| CN1176034C (en) | 2004-11-17 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN100522851C (en) | Anaerobic-aerobic-film processing technique for urban domestic refuse percolate | |
| CN100398470C (en) | Infiltration method for treating garbage | |
| CN103641272B (en) | High concentrated organic wastewater and percolate zero-discharge treatment system | |
| CN100509664C (en) | Method for treating percolation liquid of water deficiency area garbage embedding field | |
| CN102557349B (en) | Process and device of low energy consumption sewage treatment based on carbon source recovery | |
| CN109336325B (en) | Device and method for zero-emission treatment of late landfill leachate | |
| CN110143725A (en) | Mixing sludge fermentation liquid is that carbon source continuous flow short-cut denitrification couples anaerobic ammonia oxidation process Treating Municipal Sewage device and method | |
| CN101870543A (en) | Landfill percolate treatment novel process | |
| CN102190400A (en) | Method for applying integrated technology of combination of membrane biochemistry and nanofiltration membrane to high-density leachate advanced treatment and recycling | |
| CN100575282C (en) | Refuse leachate treatment technology | |
| CN1176034C (en) | Process and apparatus for urban refuse cite penetrating liquid by three stage plus one process | |
| CN103723884B (en) | The sewage water treatment method of a kind of COD that degrades, BOD, SS, ammonia nitrogen | |
| CN101054250A (en) | Technique for treating garbage percolate by combinated physicochemistry and organism bacterium | |
| CN101125724A (en) | Innocuous treatment method for mature landfill leachate | |
| CN116062891A (en) | Sectional type A 2 Combined sludge resource utilization system for O sewage treatment | |
| CN101805089A (en) | Composite treatment method of garbage percolate | |
| CN111253001A (en) | Domestic sewage treatment device and treatment method thereof | |
| CN106673362A (en) | Combined treatment process of landfill leachate | |
| CN108033555B (en) | Method for quickly starting anaerobic biological treatment system of leachate of waste incineration plant | |
| CN111875171B (en) | Duck breeding wastewater treatment process and resource recovery method | |
| CN1193943C (en) | Garbage infiltration liquid treating method | |
| CN105502852A (en) | Method for quickly treating refuse leachate of refuse incineration plant | |
| CN112919736A (en) | Anaerobic denitrification and methane removal device and method, sewage treatment system and method | |
| CN107662976A (en) | A kind of method of fulvic acid in efficient anaerobic degraded waste incineration leachate | |
| CN101323488B (en) | Method for improving sewerage dephosphorization and denitrification effect |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C41 | Transfer of patent application or patent right or utility model | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20090213 Address after: Beijing City, Haidian District Zizhuyuan Road No. 81 hospital 10 Mingdi A 303 Patentee after: Beijing Haili hi tech Environmental Protection Technology Co Ltd Address before: Lin tower, 132 Lianhua Road East, West Railway Station, Beijing Patentee before: Zhaolin Environment Technology Development Co., Beijing |
|
| ASS | Succession or assignment of patent right |
Owner name: BEIJING HAILI GAOKE ENVIRONMENTAL PROTECTION TECHN Free format text: FORMER OWNER: BEIJING ZHAOLIN ENVIRONMENTAL TECHNOLOGICAL DEVELOPMENT CO. Effective date: 20090213 |
|
| C17 | Cessation of patent right | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20041117 Termination date: 20100328 |