CN102617004A - Sewage treatment system for developing and applying carbon source by using authigenic sludge - Google Patents
Sewage treatment system for developing and applying carbon source by using authigenic sludge Download PDFInfo
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- CN102617004A CN102617004A CN2012101180500A CN201210118050A CN102617004A CN 102617004 A CN102617004 A CN 102617004A CN 2012101180500 A CN2012101180500 A CN 2012101180500A CN 201210118050 A CN201210118050 A CN 201210118050A CN 102617004 A CN102617004 A CN 102617004A
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Abstract
The invention relates to a sewage treatment system for developing and applying a carbon source by using authigenic sludge. The sewage treatment system comprises a pretreatment tank, wherein a water outlet of the pretreatment tank is sequentially connected with a biological reaction tank and a secondary sedimentation tank; a supernatant output port of the secondary sedimentation tank is connected with a water outlet pipe; and a sludge output port of the secondary sedimentation tank is connected to a water inlet of the biological reaction tank through a sludge return pipe. The sewage treatment system is characterized in that: an ozone sludge wall breaking device is also connected between the sludge output port of the secondary sedimentation tank and the water inlet of the biological reaction tank through a wall-breaking sludge return pipe; the device consists of an ozone generator, a gas-water mixer, a gas flowmeter, a liquid flowmeter and a sludge pump, and the ozone generator is connected with an air inlet of the gas-water mixer through the gas flowmeter; an output port of the sludge pump which is connected with the secondary sedimentation tank is connected with a liquid inlet of the gas-water mixer through the liquid flowmeter; and a liquid outlet of the gas-water mixer is connected with the water inlet of the biological reaction tank. The sewage treatment system has the advantages that: the problem of the shortage of the carbon source in sewage treatment is solved, resources are saved, and the environment is protected.
Description
Technical field
The present invention relates to technical field of sewage, relate in particular to a kind of being mainly used in and carry out carbon source exploitation and the Sewage treatment systems of using from raw sludge as the utilization of the town sewage processing usefulness of sewage treatment process with activated sludge process.
Background technology
Activated sludge process has been widely used in municipal sewage treatment, and this discharging for nitrogen and phosphorus in the reduction sewage, protection water body environment play a role.Traditional active sludge processing system mainly comprises pretreatment pool, biological reaction tank, the second pond that connects successively; Sewage is impurity such as the inorganics in pretreatment pool removal sewage, silt particle at first; Get into biological reaction tank removal organism and nitrogen, phosphorus again; Get into second pond at last and carry out mud-water separation, the mud part after the separation is returned biological reaction tank as bacterial classification, and all the other mud are discharged as refuse.The defective that present activated sludge process is used for the municipal sewage treatment existence is: the effect of biological carbon and phosphorous removal is often advanced the influence of water COD, when the COD in the sewage is low, nitrogen phosphorus can occurs and remove unfavorable phenomenon.For reducing the nitrogen phosphorus in the water outlet, adding outer carbon source is a kind of effective means.Through discovering in a large number, can improve the denitrogenation dephosphorizing effect greatly at sewage treatment process interpolation acetate in service, methyl alcohol etc., but its defective is to consume human limited organic resource, and can increases the processing cost of sewage work greatly.In addition, adopt Wastewater Treated by Activated Sludge Process sewage, in operational process, can produce a large amount of excess sludges,, will cause secondary pollution like untimely processing.
Material in the mud in the microorganism cells exist like the form of the materials more than 95% such as many carbon sugar, fat, protein and nucleic acid with COD, and ozone is as a kind of strong oxidizer; Have sterilization virus killing effect, if can utilize ozone that above-mentioned excess sludge is carried out oxide treatment, the destroy microorganisms cell; Make it discharge intracellular organic substance; With changing waste into valuable, rationally utilize these excess sludges, the problem of the biosystem denitrogenation dephosphorizing poor effect that solution water-inlet carbon source deficiency causes; Help environment protection, economize on resources, and will produce material impact the sustainable development of sewage treatment industry.
Summary of the invention
Main purpose of the present invention is to the problems referred to above; Provide a kind of utilization to carry out carbon source exploitation and the Sewage treatment systems of using from raw sludge; Obtain carbon source through utilizing in the sewage treatment process product mud of self to carry out broken wall, solve the insufficient problem of carbon source in the WWT, the protection environment; Economize on resources, realize sewage work's qualified discharge.
The technical solution adopted for the present invention to solve the technical problems is:
A kind of utilization from raw sludge carried out carbon source exploitation and the Sewage treatment systems of using; Comprise the pretreatment pool that connects water inlet pipe; The pretreatment pool water outlet connects biological reaction tank and second pond successively; The supernatant delivery port of said second pond connects rising pipe; The mud delivery port of second pond is connected to the water-in of biological reaction tank through mud return line, it is characterized in that between the water-in of the mud delivery port of said second pond and biological reaction tank, also connecting an ozone mud means for breaking walls through the broken wall mud return line.
Said ozone mud means for breaking walls is to take into account sludge pump by ozonizer, gas-water mixer, gas meter, liquid flow rate to constitute, and said ozonizer connects the inlet mouth of said gas-water mixer through gas meter; The input aperture of said sludge pump is through the mud delivery port of broken wall mud return line connection second pond, and the delivery port of sludge pump connects the fluid inlet of gas-water mixer through said liquid meter; The liquid outlet of gas-water mixer is connected to the water-in of biological reaction tank through the broken wall mud return line.
The invention has the beneficial effects as follows: ozone mud means for breaking walls is set in traditional activated sludge sewage processing system, and ozone mud means for breaking walls comprises ozonizer, gas-water mixer; Carry out in the contact process at excess sludge and ozone; Strong oxidizing property through ozone is bored a hole to microorganism wall, and the cell walls of destroy microorganisms causes cytoplasmic release, and COD discharges from cell interior through ruined cell walls; Be added in the biological reaction tank as carbon source; This part COD does not need additional carbon with the problem that solves the biosystem denitrogenation dephosphorizing poor effect that the water-inlet carbon source deficiency causes, and has realized sewage work's qualified discharge; Economize on resources the protection environment.Ozone mud broken wall system operation is simple, and operation expense is low; Be applicable to the newly-built and reconstruction and extension project of the technologies of deriving such as conventional activated sludge process and A/A/O, A/O, SBR, oxidation ditch, effect is actively promoted in the sustainable development generation of sewage treatment industry.
Description of drawings
Fig. 1 is a structural representation of the present invention.
Among the figure: 1 water inlet pipe, 2 pretreatment pools, 3 biological reaction tanks, 4 second ponds, 5 rising pipes, 6 mud return lines, 7 sludge pumps, 8 liquid meters, 9 gas-water mixers, 10 broken wall mud return lines, 11 gas meters, 12 ozonizers, A ozone mud means for breaking walls.
Below in conjunction with accompanying drawing and embodiment to the detailed description of the invention.
Embodiment
Fig. 1 illustrates a kind of utilization and carries out carbon source exploitation and the Sewage treatment systems of using from raw sludge; Comprise the pretreatment pool 2 that connects water inlet pipe 1; The water outlet of pretreatment pool 2 connects biological reaction tank 3 and second pond 4 successively; The supernatant delivery port of second pond connects rising pipe 5; The mud delivery port of second pond is connected to the water-in of biological reaction tank 3 through mud return line 6, it is characterized in that also connecting an ozone mud means for breaking walls A through broken wall mud return line 10 between the water-in of mud delivery port and biological reaction tank 3 of above-mentioned second pond 4.Said ozone mud means for breaking walls A is made up of ozonizer 12, gas-water mixer 9, gas meter 11, liquid meter 8 and sludge pump 7, and above-mentioned ozonizer 12 connects the inlet mouth of gas-water mixer 9 through gas meter 11; The input aperture of sludge pump 7 is through the mud delivery port of broken wall mud return line 10 connection second ponds 4, and the delivery port of sludge pump 7 connects the fluid inlet of gas-water mixers 9 through liquid meter 8; The liquid outlet of gas-water mixer 9 is connected to the water-in of biological reaction tank 3 through broken wall mud return line 10.
Above-mentioned gas-water mixer 9, ozonizer 8 all adopt the commercially available prod.In the present embodiment, the model that ozonizer has adopted Qingdao Guolin Industry Co., Ltd. to produce is the ozonizer of CF-G-200G.Gas-water mixer is conventional jet gas-water mixer.Gas meter 11 and liquid meter 8 also are conventional flow instrument.
When system moves; Identical with traditional active sludge Sewage treatment systems technology, sewage is impurity such as the inorganics in water inlet pipe 1 entering pretreatment pool 2 removal sewage, silt particle at first, get into biological reaction tank 3 removal organism and nitrogen, phosphorus again; Get into second pond 4 at last and carry out solid-liquid separation; Supernatant after the separation is from rising pipe 5 outputs, and a mud part is returned biological reaction tank 3 as bacterial classification through mud return line 6, and excess sludge is discharged.Characteristics of the present invention are on above-mentioned traditional active sludge Sewage treatment systems basis, to improve; Between the water-in of the mud delivery port of second pond 4 and biological reaction tank 3, set up the ozone mud means for breaking walls A that comprises ozonizer 12 and gas-water mixer 9; And through broken wall mud return line 10 broken wall mud is turned back in the biological reaction tank 3, be the denitrogenation dephosphorizing supplementary carbon source of biosystem.
To handle municipal wastewater is example; In excess sludge discharge, sludge pump 7 and liquid meter 8 through being provided with on the broken wall mud return line 10 are drawn into the mud delivery port of a part of excess sludge from second pond 4 gas-water mixer 9 by set amount; General excess sludge concentration MLSS is 7000-10000mg/L; The sludge quantity that carries out broken wall by volume, is equivalent to the 2-10% of system's flooding quantity according to the influent quality situation; The ozone concn that ozonizer 12 produces is controlled at 18-22mg/L, and the ozone amount of feeding is controlled through gas meter 11; The air water volume ratio of ozone and mud is 0.2-0.8: 1; Ozone contacts mixing with mud in gas-water mixer 9; Because the strong oxidizing property of ozone is bored a hole to microorganism wall, the cell walls of destroy microorganisms causes cytoplasmic release; COD discharges from cell interior through ruined cell walls; Be added in the biological tank 3 through broken wall mud return line 10 as carbon source, thereby be biological denitrogenation dephosphorizing supplementary carbon source, realized the denitrogenation dephosphorizing operation up to standard of Sewage Plant.Table 1 shows application example of the present invention and effect.
Table 1 utilizes the application example that carries out the Sewage treatment systems of carbon source exploitation and application from raw sludge
The COD of water-in and water-out, TN, TP and NH in the above-mentioned table 1
3-N desired value is to test acquisition according to GB18918-2002 " urban wastewater treatment firm pollutant emission standard ".Can find out with the Comparative Examples contrast of adopting conventional art through above embodiment 1-3; Adopt Sewage treatment systems provided by the invention; Owing to increased organic content in the sewage, nitrogen phosphorus removal amount significantly improves, with the conventional art ratio; TN content reduces more than 30% in the water outlet, and TP content is reduced to original 5.7%; NH
3-N content is minimum reduces to originally 50%, obtains the process well effect.
Above content is not that structure of the present invention, shape are done any pro forma restriction.Every foundation technical spirit of the present invention all still belongs in the scope of technical scheme of the present invention any simple modification, equivalent variations and modification that above embodiment did.
Claims (2)
1. a utilization is carried out carbon source exploitation and the Sewage treatment systems of using from raw sludge; Comprise the pretreatment pool that connects water inlet pipe; The pretreatment pool water outlet connects biological reaction tank and second pond successively; The supernatant delivery port of said second pond connects rising pipe; The mud delivery port of second pond is connected to the water-in of biological reaction tank through mud return line, it is characterized in that between the water-in of the mud delivery port of said second pond and biological reaction tank, also connecting an ozone mud means for breaking walls through the broken wall mud return line.
2. a kind of the utilization from raw sludge according to claim 1 carried out carbon source exploitation and the Sewage treatment systems of using; It is characterized in that said ozone mud means for breaking walls is to take into account sludge pump by ozonizer, gas-water mixer, gas meter, liquid flow rate to constitute, said ozonizer connects the inlet mouth of said gas-water mixer through gas meter; The input aperture of said sludge pump is through the mud delivery port of broken wall mud return line connection second pond, and the delivery port of sludge pump connects the fluid inlet of gas-water mixer through said liquid meter; The liquid outlet of gas-water mixer is connected to the water-in of biological reaction tank through the broken wall mud return line.
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| CN2012101180500A CN102617004A (en) | 2012-04-19 | 2012-04-19 | Sewage treatment system for developing and applying carbon source by using authigenic sludge |
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Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104211237A (en) * | 2014-08-22 | 2014-12-17 | 天津未来生物技术发展有限公司 | Advanced treatment device for ozonized wastewater |
| CN104478074A (en) * | 2014-12-31 | 2015-04-01 | 天津凯英科技发展有限公司 | Sewage denitrification system and method |
| WO2015081658A1 (en) * | 2013-12-03 | 2015-06-11 | 南京德磊科技有限公司 | Sludge treatment system and method therefor |
| CN105347474A (en) * | 2015-12-03 | 2016-02-24 | 安徽锋亚环境技术有限公司 | Sewage treatment system adopting excess sludge to supplement carbon source |
| CN105621814A (en) * | 2016-03-07 | 2016-06-01 | 北京恩菲环保股份有限公司 | High-quality regenerated recycle water treatment system and method |
| CN106915861A (en) * | 2015-12-24 | 2017-07-04 | 中国科学院过程工程研究所 | A kind of coal chemical industrial waste water biological treatment system and its processing method based on sludge ozone catalysis oxidation |
| CN114906923A (en) * | 2022-05-24 | 2022-08-16 | 山西瑞成达生环科技有限公司 | Method for electrically controlling release of solid carbon source |
Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2008086848A (en) * | 2006-09-29 | 2008-04-17 | Kurita Water Ind Ltd | Apparatus and method for treating organic liquid waste |
| CN201962168U (en) * | 2011-01-14 | 2011-09-07 | 北京工商大学 | System for strengthening denitrification and dephosphorization effects of A2/O process |
| CN202499751U (en) * | 2012-04-19 | 2012-10-24 | 天津凯英科技发展有限公司 | Sewage treatment system of developing and applying carbon source by utilizing self-generated sludges |
-
2012
- 2012-04-19 CN CN2012101180500A patent/CN102617004A/en active Pending
Patent Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2008086848A (en) * | 2006-09-29 | 2008-04-17 | Kurita Water Ind Ltd | Apparatus and method for treating organic liquid waste |
| CN201962168U (en) * | 2011-01-14 | 2011-09-07 | 北京工商大学 | System for strengthening denitrification and dephosphorization effects of A2/O process |
| CN202499751U (en) * | 2012-04-19 | 2012-10-24 | 天津凯英科技发展有限公司 | Sewage treatment system of developing and applying carbon source by utilizing self-generated sludges |
Non-Patent Citations (1)
| Title |
|---|
| 曾绍琼等: "无剩余污泥的活性污泥法", 《造纸科学与技术》 * |
Cited By (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2015081658A1 (en) * | 2013-12-03 | 2015-06-11 | 南京德磊科技有限公司 | Sludge treatment system and method therefor |
| US9771293B2 (en) | 2013-12-03 | 2017-09-26 | Nanjing Delei Science & Technology Co., Ltd. | Sludge treatment system |
| CN104211237A (en) * | 2014-08-22 | 2014-12-17 | 天津未来生物技术发展有限公司 | Advanced treatment device for ozonized wastewater |
| CN104478074A (en) * | 2014-12-31 | 2015-04-01 | 天津凯英科技发展有限公司 | Sewage denitrification system and method |
| CN105347474A (en) * | 2015-12-03 | 2016-02-24 | 安徽锋亚环境技术有限公司 | Sewage treatment system adopting excess sludge to supplement carbon source |
| CN106915861A (en) * | 2015-12-24 | 2017-07-04 | 中国科学院过程工程研究所 | A kind of coal chemical industrial waste water biological treatment system and its processing method based on sludge ozone catalysis oxidation |
| CN105621814A (en) * | 2016-03-07 | 2016-06-01 | 北京恩菲环保股份有限公司 | High-quality regenerated recycle water treatment system and method |
| CN105621814B (en) * | 2016-03-07 | 2018-09-11 | 北京恩菲环保股份有限公司 | High-quality regeneration water treatment system and method |
| CN114906923A (en) * | 2022-05-24 | 2022-08-16 | 山西瑞成达生环科技有限公司 | Method for electrically controlling release of solid carbon source |
| CN114906923B (en) * | 2022-05-24 | 2023-03-10 | 山西瑞成达生环科技有限公司 | Method for electrically controlling release of solid carbon source |
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Application publication date: 20120801 |