CN102173537A - Integrated biochemical filtering sewage treatment apparatus - Google Patents
Integrated biochemical filtering sewage treatment apparatus Download PDFInfo
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- CN102173537A CN102173537A CN 201110061307 CN201110061307A CN102173537A CN 102173537 A CN102173537 A CN 102173537A CN 201110061307 CN201110061307 CN 201110061307 CN 201110061307 A CN201110061307 A CN 201110061307A CN 102173537 A CN102173537 A CN 102173537A
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Abstract
The invention discloses an integrated biochemical filtering sewage treatment apparatus, belonging to the field of sewage treatment. The integrated biochemical filtering sewage treatment apparatus comprises a treating pool and a V-shaped sludge bed filter in the treating pool, wherein the V-shaped sludge bed filter divides the treating pool into a facultative/anaerobic area and an aerobic reaction area. The integrated biochemical filtering sewage treatment apparatus is suitable for the fields of municipal sewage, domestic sewage, industrial sewage and the like, which not only can be applied to large-scale sewage centralized treatment, but also is applicable to small-scale disperse sewage treatment such as rural areas, residential areas, tourist attractions and the like.
Description
Technical field
The present invention relates to a kind of integrated biochemistry filtered sewage disposal device, be exactly that one is become in a kind of biological treatment and Sludge Bed filtration with denitrogenation dephosphorizing specifically, the sewage disposal device that promptly integrates double oxygen/anaerobic pond, aerobic reaction pond and sludge filtration bed, be applicable to fields such as municipal wastewater, sanitary sewage, industrial sewage, not only can be used for large-scale sewage focuses on, more can be applicable to small-sized decentralized wastewater processing, as rural area, sub-district, tourist attractions etc.
Background technology
Increasingly stringent along with sewage drainage standard, not only require to have higher organic matter removal efficient, also require to have higher denitrogenation dephosphorizing effect, denitrogenation dephosphorizing is a great problem of sewage treatment area, if effect is bad, directly enter environment water, can make environment water produce hydrobiological wawter bloom of serious harm or red tide because of eutrophication.Large-scale wastewater treatment plant generally adopts CASS, oxidation ditch etc. to have the technology of denitrogenation dephosphorizing function, all have double oxygen/anaerobic pond and aerobic reaction tank, but small-scale sewage is handled and is then generally adopted aerobic process, the function that does not have denitrogenation dephosphorizing, it is big to have floor space if employing has the technology of denitrogenation dephosphorizing function, defectives such as manufacturing cost height, and all be arranged with the filter plant branch, equipment and initial cost more increased.Traditional Sludge Bed is filtered the general columnar structure that adopts, and there is the dead band in mud-water separation, and efficient has much room for improvement.
Summary of the invention
The objective of the invention is to overcome or improve the shortcoming of prior art, a kind of compact construction, low cost of manufacture, sewage disposal device that treatment effect is good are provided, the biochemical process and the Sludge Bed filtration of denitrogenation dephosphorizing are combined, technical process is simple, can resist to impact and meet, traditional mud-water separation means have particularly been changed, have mud-water separation efficient and extraordinary effluent quality more efficiently, and be easy to the integrated sewage treating apparatus that seriation and modularization are produced, not only can be used for large-scale sewage and focus on, more can be applicable to small-sized decentralized wastewater processing.
The integrated biochemistry filtered sewage disposal device of the present invention, it is characterized in that in treating pond, being provided with V-arrangement Sludge Bed strainer, V-arrangement Sludge Bed strainer is separated into treating pond double/anaerobic zone, aerobic reactor zone, between the bottom of described Sludge Bed strainer and the treating pond bottom certain interval is arranged, bottom at the Sludge Bed strainer is provided with the Sludge Bed water-in near aerobic zone one side, the bottom of V-arrangement Sludge Bed strainer is provided with mud return line, mud return line connects reflux pump, mud is back to the place suitable for reading of double oxygen/anaerobic zone, the bottom of aerobic zone is provided with aerating apparatus, the place suitable for reading of Sludge Bed strainer is provided with the water outlet overflow device, and overflow device bottom is provided with rising pipe.
Description of drawings
Fig. 1 is the synoptic diagram of an embodiment of the present invention.
Embodiment
The integrated biochemistry filtered sewage disposal device that the present invention proposes comprises treating pond 1, the inlet that sewage enters treating pond is 12, V-arrangement Sludge Bed strainer 5 is set in treating pond, its inside is mud-water separation district 4, V-arrangement Sludge Bed strainer 5 is separated into treating pond double/anaerobic zone 2, aerobic reactor zone 3, between the bottom of V-arrangement Sludge Bed strainer and the treating pond bottom certain interval is arranged, the bottom of Sludge Bed strainer is provided with Sludge Bed water-in 6 near aerobic zone one side, the bottom of Sludge Bed strainer is provided with mud return line 7, mud return line connects reflux pump 8, mud is back to the place suitable for reading of double oxygen/anaerobic zone, the bottom of aerobic zone is provided with aerating apparatus 11, the place suitable for reading of Sludge Bed strainer is provided with water outlet overflow device 9, has rising pipe 10 under the overflow device.Below in conjunction with embodiment and accompanying drawing the utility model is described in detail.
The present invention is in practice, the sewage disposal flow process is as follows: simple pretreated sewage through inlet enter double oxygen/anaerobic zone and with the active sludge thorough mixing that refluxes from V-arrangement Sludge Bed filter bottom, behind the oxygen/anaerobic zone of holding concurrently, the gap that from the bottom is V-arrangement Sludge Bed strainer and treating pond bottom enters aerobic reactor zone, enter V-arrangement Sludge Bed strainer through the mud of aeration aerobic treatment and the mixed solution of water from the Sludge Bed water-in, biofiltration and throwing out take place in the Sludge Bed strainer, in the process of upper reaches, micropopulation increases gradually and constantly slows down until the micropopulation transfixion, forming one deck filtration medium is Sludge Bed, and separating and filtering efficient is improved greatly.After the mud-water separation, clear water enters overflow weir and discharges reactor, and active sludge then is back to double oxygen/anaerobic zone by Sludge Bed filter bottom collection tube, the Sludge Bed strainer is the V-arrangement upward flow, and along with the rising of current, flow velocity slows down gradually, more help mud-water separation, efficient improves greatly.
The present invention is integrated biochemistry filtered sewage disposal device, and double oxygen/anaerobic pond, aerobic reaction pond and Sludge Bed strainer are combined, and has changed the traditional wastewater biochemical treatment and has filtered the mode that is arranged of dividing.Adopt integration apparatus, and the traditional filtration means of the change of filter plant wherein, but adopt upward flow V-arrangement Sludge Bed to filter, separation efficiency is improved greatly.Be applicable to fields such as municipal wastewater, sanitary sewage, industrial sewage, not only can be used for large-scale sewage to focus on, more can be applicable to small-sized decentralized wastewater processing, as rural area, sub-district, tourist attractions etc.
Principal feature of the present invention is embodied in following several respects.
1, wastewater treatment efficiently not only can be removed common organism, effectively reduces BOD, COD, and has the effect of denitrogenation dephosphorizing, and the aerobic area of sludge filtration bed provides necessary condition by " nutraceutical picked-up " for denitrogenation dephosphorizing.Oxygen compatibility pool provides favourable condition as " selecting the district " for settleability and the hyphomycetic growth of control that improves mixed solution.
2, investment and running cost are low, compare with existing more advanced technology such as SBR, oxidation ditch, needed mechanical assist device, electricity needs, monitoring requirement etc. are all lower, so be that initial cost of investment or later running cost all greatly reduces.
3, moudle type flexible design, Sludge Bed strainer wherein can be used as newly-built equipment, also can reconstruct existing reaction tank, adopts multiple material to be retrofitted in the existing treating pond and uses.
4, floor space is little, and this equipment collection is nitrated, denitrogenation, precipitation and to stablize the mud process be one, has reduced the requirement to connecting between the equipment, has dwindled the floor space of whole plant.
The present invention determines by experiment, and the optimum operation controlled variable of handling municipal wastewater is as follows: oxygen-starved area DO＜0.1mg/L, and aerobic zone DO is at 2.0～4.0mg/L, PH should remain on 7.0-8.5, return sludge ratio R=200%, total HRT=8h(aerobic zone 6h, oxygen-starved area 2h), SRT=15d.At this moment, COD on average goes out water concentration below 50mg/L, and ammonia nitrogen approaches 0mg/L, and TN is about 5mg/L, and TP is below 0.5mg/L, and effluent quality reaches (GB18918-2002) one-level category-A standard of country's " urban wastewater treatment firm pollutant emission standard ".COD, ammonia nitrogen and TP average removal rate are all more than 90%.Because the biofiltration and the throwing out of V-arrangement upward flow sludge filtration bed, water outlet is very limpid, and near tap water, SS is almost nil, NTU=2～3.
Claims (1)
1. integrated biochemistry filtered sewage disposal device, it is characterized in that in treating pond, being provided with V-arrangement Sludge Bed strainer, V-arrangement Sludge Bed strainer is separated into treating pond double/anaerobic zone, aerobic reactor zone, between the bottom of described Sludge Bed strainer and the treating pond bottom certain interval is arranged, bottom at the Sludge Bed strainer is provided with the Sludge Bed water-in near aerobic zone one side, the bottom of V-arrangement Sludge Bed strainer is provided with mud return line, mud return line connects reflux pump, mud is back to the place suitable for reading of double oxygen/anaerobic zone, the bottom of aerobic zone is provided with aerating apparatus, the place suitable for reading of Sludge Bed strainer is provided with the water outlet overflow device, and overflow device bottom is provided with rising pipe.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201110061307 CN102173537A (en) | 2011-03-15 | 2011-03-15 | Integrated biochemical filtering sewage treatment apparatus |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201110061307 CN102173537A (en) | 2011-03-15 | 2011-03-15 | Integrated biochemical filtering sewage treatment apparatus |
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| CN102173537A true CN102173537A (en) | 2011-09-07 |
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| CN 201110061307 Pending CN102173537A (en) | 2011-03-15 | 2011-03-15 | Integrated biochemical filtering sewage treatment apparatus |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105384313A (en) * | 2015-12-12 | 2016-03-09 | 宋丽娜 | Integrated water treatment apparatus |
| CN108862832A (en) * | 2018-06-25 | 2018-11-23 | 安徽建筑大学 | Method and reactor for integrally purifying micro-polluted source water by using micro-flocculation biological carbon biomembrane AO |
Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN2793062Y (en) * | 2005-03-09 | 2006-07-05 | 哈尔滨工业大学环保科技股份有限公司 | Integrated biological sewage denitrifying descaling apparatus |
| US20080073265A1 (en) * | 2004-09-10 | 2008-03-27 | Paques B.V. | Process for the Simultaneous Removal of Bod and Phosphate from Waste Water |
| CN201598224U (en) * | 2009-12-30 | 2010-10-06 | 浦华环保有限公司 | Biological nitrogen and phosphorus removal treatment and filter integrated sewage treatment system |
| CN201981100U (en) * | 2011-03-15 | 2011-09-21 | 北京科泰兴达高新技术有限公司 | Integral biochemical filtering sewage processing equipment |
-
2011
- 2011-03-15 CN CN 201110061307 patent/CN102173537A/en active Pending
Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US20080073265A1 (en) * | 2004-09-10 | 2008-03-27 | Paques B.V. | Process for the Simultaneous Removal of Bod and Phosphate from Waste Water |
| CN2793062Y (en) * | 2005-03-09 | 2006-07-05 | 哈尔滨工业大学环保科技股份有限公司 | Integrated biological sewage denitrifying descaling apparatus |
| CN201598224U (en) * | 2009-12-30 | 2010-10-06 | 浦华环保有限公司 | Biological nitrogen and phosphorus removal treatment and filter integrated sewage treatment system |
| CN201981100U (en) * | 2011-03-15 | 2011-09-21 | 北京科泰兴达高新技术有限公司 | Integral biochemical filtering sewage processing equipment |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105384313A (en) * | 2015-12-12 | 2016-03-09 | 宋丽娜 | Integrated water treatment apparatus |
| CN108862832A (en) * | 2018-06-25 | 2018-11-23 | 安徽建筑大学 | Method and reactor for integrally purifying micro-polluted source water by using micro-flocculation biological carbon biomembrane AO |
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Application publication date: 20110907 |