CN202499759U - Anaerobic hydrolysis system for treating wastewater difficult to degrade biochemically - Google Patents
Anaerobic hydrolysis system for treating wastewater difficult to degrade biochemically Download PDFInfo
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- CN202499759U CN202499759U CN 201120503742 CN201120503742U CN202499759U CN 202499759 U CN202499759 U CN 202499759U CN 201120503742 CN201120503742 CN 201120503742 CN 201120503742 U CN201120503742 U CN 201120503742U CN 202499759 U CN202499759 U CN 202499759U
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Abstract
The utility model discloses an anaerobic hydrolysis system for treating wastewater difficult to degrade biochemically. The anaerobic hydrolysis system is characterized in that an anaerobic hydrolyzer, a first water passing pipe, an aerobic device, a second water passing pipe and a secondary sedimentation device are connected in order; anaerobic hydrolysis catalyst fillers are arranged in the middle of the anaerobic hydrolyzer; water distributors are arranged at the bottom of the anaerobic hydrolyzer; a water inlet pump, a valve and the water distributors are connected in order; a mixed liquid reflux pump is arranged outside the anaerobic hydrolyzer; aeration systems are arranged at the bottom of the aerobic device and are connected with a blower; an outlet at the bottom of the secondary sedimentation device is connected with the bottom of the aerobic device via a secondary sedimentation region sludge reflux pump through a sludge reflux pipe; and a water outlet pipe is arranged on the upper part of the secondary sedimentation device. The anaerobic hydrolysis system has the following beneficial effects: a process adopting the anaerobic hydrolysis device is suitable for all wastewater difficult to degrade biochemically, such as printing and dyeing wastewater, medical and chemical wastewater, papermaking wastewater, landfill leachate wastewater and coking wastewater, and can be used for treating the wastewater difficult to degrade biochemically in the new wastewater treatment engineering and reconstructing the built engineering.
Description
Technical field
The utility model relates to field of environment engineering technology, relates in particular to a kind of anaerobic hydrolysis system that handles bio-refractory waste water.
Background technology
Along with the quickening propelling of city process, a large amount of development of industrial enterprise, in addition; Country and enterprise are to the more and more attention of environment protection, the synchronization implementation of cleaner production, the enforcement of national pollution emission reduction policy; Make some industrial enterprises pay attention to cleaner production; Reduce the generation of wastewater flow rate, make the concentration of waste water increase the also corresponding increase of the difficulty of wastewater treatment.The organic pollutant of these high densitys, bio-refractory can remain in the water body after getting into water body for a long time, has stronger toxicity and carcinogenic, mutagenesis, and through food chain accumulation, enrichment, finally gets into toxigenicity in animal or human's body.The poisonous and harmful trade effluent of high density, bio-refractory, it is up to standard to adopt existing conventional process method to be difficult to, and must develop pointed, reliable novel treatment technology.Along with the increasingly stringent of National Environment Policy Act rule, country and local government will propose higher requirement to enterprise's externally discharged waste water emission standard.And draining generally has the characteristics of low COD (about 100mg/L), low B/C value, difficult biochemical treatment outside the present industrial enterprise, and this just requires to develop efficiently, advanced treatment of wastewater is technological cheaply, to adapt to the environmental requirement of increasingly stringent.
Anaerobic hydrolysis technology is through the control acidization; Utilize the anaerobion in the mud; Can the larger molecular organics of non-molten attitude or difficult degradation in the waste water be converted into and dissolve the small organic molecule that attitude is prone to degraded; Therefore significantly improve the biodegradability of waste water, be applied to more and more in the pre-treatment of various used water difficult to degradate, and have that excess sludge production is few, energy consumption is low, advantage such as simple to operate, effect stability.Show that through secular practical studies the principal element that influences the acidication processing efficiency is: the homogeneity and the muddy water blended adequacy of water inlet water distribution.So the key that improves the anaerobic hydrolysis technology is to handle this two kinds of principal elements well.For this reason, scientist has gone out multiple different form to the form Study of acidication and has remedied above deficiency.The arrangement form of acidication can be divided into: flow lifting type, pulling flow type and deflector type.Various reactive modes differ from one another also respectively has shortcoming.A kind of anaerobic hydrolysis device of handling bio-refractory waste water of exploitation is still a focus in environmental protection field at present.
Summary of the invention
The purpose of the utility model is the deficiency that overcomes prior art, and a kind of anaerobic hydrolysis system that handles bio-refractory waste water is provided.
The anaerobic hydrolysis system that handles bio-refractory waste water comprises that intake pump, valve, water distributor, anaerobic hydrolysis catalyst filling, anaerobic hydrolysis tower, first cross water pipe, gas blower, aerobic device, aerating system, second and cross water pipe, two sink devices, two heavy district sludge reflux pumps, mud return line, rising pipe and mixed-liquor return pumps; Anaerobic hydrolysis tower, first is crossed water pipe, aerobic device, second is crossed water pipe, two sink devices and linked to each other in order; Anaerobic hydrolysis tower middle part is provided with the anaerobic hydrolysis catalyst filling; The anaerobic hydrolysis tower bottom is provided with water distributor, and intake pump, valve, water distributor link to each other in order, and the anaerobic hydrolysis tower is provided with the mixed-liquor return pump outward; Aerobic bottom of device is provided with aerating system; Aerating system links to each other with gas blower, and two sink device outlet at bottoms link to each other with aerobic bottom of device through mud return line through two heavy district sludge reflux pumps, and two sink device tops are provided with rising pipe.
The beneficial effect that the utility model compared with prior art has is:
1) compactness simple for structure of the hydrolysis device in this technology, water distribution is even, and the operation operational management is convenient.
2) biodegradability of bio-refractory waste water can fully improve in the acidication workshop section in this technology, and follow-up aerobic workshop section can better be played a role.
3) in the acidication workshop section in this technology through loading the catalyzer of crossing through overactivation, more can improve the biodegradability of bio-refractory waste water.
4) this technology both can be used for newly-built sewage treatment project, also can be used for building the transformation of engineering.
Description of drawings
Fig. 1 is an anaerobic hydrolysis system architecture synoptic diagram of handling bio-refractory waste water;
Fig. 2 is the plot plan of the water distributor of the utility model.
Embodiment
As shown in Figure 1, the anaerobic hydrolysis system that handles bio-refractory waste water comprises that intake pump 1, valve 2, water distributor 3, anaerobic hydrolysis catalyst filling 4, anaerobic hydrolysis tower 5, first cross water pipe 6, gas blower 7, aerobic device 8, aerating system 9, second and cross water pipe 10, two sink devices, 11, two heavy district sludge reflux pumps 12, mud return line 13, rising pipe 14, mixed-liquor return pump 15, vapor pipe 16, valve 17, sight glass 18, manhole 19, effluent trough 20 and annular water inlet pipes 21; Anaerobic hydrolysis tower 5, first is crossed water pipe 6, aerobic device 8, second is crossed water pipe 10, two sink devices 11 and linked to each other in order; Anaerobic hydrolysis tower 5 middle parts are provided with anaerobic hydrolysis catalyst filling 4; Anaerobic hydrolysis tower 5 bottoms are provided with water distributor 3, and intake pump 1, valve 2, water distributor 3 link to each other in order, the anaerobic hydrolysis tower 5 outer mixed-liquor return pumps 15 that are provided with; Aerobic device 8 bottoms are provided with aerating system 9; Aerating system 9 links to each other with gas blower 7, and two sink devices, 11 outlet at bottoms link to each other with aerobic device 8 bottoms through mud return line 13 through two heavy district sludge reflux pumps 12, and two sink devices, 11 tops are provided with rising pipe 14.
The anaerobic hydrolysis technology of handling bio-refractory waste water is: bio-refractory waste water gets into anaerobic hydrolysis tower 5 through intake pump 1 through valve 2 water distributors 3; Bio-refractory waste water is through the anaerobic hydrolysis catalyst filling 4 in the anaerobic hydrolysis tower 5; Stop after 12～24 hours and cross the aerobic device 8 of water pipe 6 entering through first; The mud that also has warp two sink devices 9 two heavy district sludge reflux pumps 12 to reflux and come that gets into synchronously through mud return line 11; Establish aerating system 9 in the aerobic device 8, make the sewage sludge thorough mixing, bio-refractory waste water is carried out sufficient aerobic reaction; To bio-refractory waste water, anaerobic hydrolysis mainly is the biodegradability that improves waste water, reduces the concentration of sewage, alleviates follow-up aerobic load; Mixed solution in the aerobic device 8 charges into air through gas blower 7 and aerating system 9, and airborne oxygen is absorbed by the aerobic microbiological in the bio-refractory waste water, the mikrobe organic pollutant in the mixed solution of in process of growth, degrading simultaneously; Bio-refractory waste water is crossed water pipe 10 through aerobic device 8, second and is flowed into two sink devices 11; After mud-water separation; Supernatant effluxes, and two sink device mud are back to aerobic device 8 bottoms, excess sludge decontamination mud treatment system through two heavy district sludge reflux pumps 12 through mud return line 11; Mixed solution through 12～24 hours anaerobic hydrolysis towers 5 is back to anaerobic hydrolysis tower 5 inlet areas through mixed-liquor return pump 15 simultaneously.
Described anaerobic hydrolysis catalyst filling 4 is to be carrier with aluminum oxide, zeolite, activated-carbon catalyst; Through immersion, load, sintering process loaded Cu, Cs, Mn, Fe, Ni, Zn metallic element, promote anaerobic hydrolysis to improve the purpose of wastewater biodegradability and decolouring to reach.
Described bio-refractory waste water is used water difficult to degradate such as dyeing waste water, doctorization waste water, paper waste, percolate waste water, coking chemical waste water.
The waste water that gets into technology is synthesis pharmaceutical class industrial sewage, and sewage quality is pH:6～8, CODcr:4000～7000mg/l, NH<sub >3</sub>-N:45～90mg/l, TP:2～6mg/l, colourity: 256 times, water temperature is a normal temperature, and the water yield is 500m<sup >3</sup>/ d, after materialization, biochemical treatment, CODcr:200～400mg/l; For reaching COD<the index of 100mg/>l, increasing sewage treatment process is that anaerobic hydrolysis+O pond+two are heavy, water outlet reaches processing requirements: CODcr basically:<100mgl.
The waste water that gets into technology is for passing through the percolate of biochemical treatment, CODcr:500～800mg/l, ammonia nitrogen: 200～300mg/l, colourity: 128 times.Sewage adopts the heavy art breading of anaerobic hydrolysis+O pond+two, and anaerobic hydrolysis stops 24h, and the aerobic zone residence time is 18h; Water outlet reaches processing requirements: CODcr＜100mg/l, ammonia nitrogen＜15mg/l, colourity＜32 times.
Claims (1)
1. an anaerobic hydrolysis system that handles bio-refractory waste water is characterized in that comprising that water pipe (6), gas blower (7), aerobic device (8), aerating system (9), second are crossed water pipe (10), two sink devices (11), two heavy district sludge reflux pumps (12), mud return line (13), rising pipe (14) and mixed-liquor return pumps (15) excessively for intake pump (1), valve (2), water distributor (3), anaerobic hydrolysis catalyst filling (4), anaerobic hydrolysis tower (5), first; Anaerobic hydrolysis tower (5), first is crossed water pipe (6), aerobic device (8), second is crossed water pipe (10), two sink devices (11) and linked to each other in order; Anaerobic hydrolysis tower (5) middle part is provided with anaerobic hydrolysis catalyst filling (4); Anaerobic hydrolysis tower (5) bottom is provided with water distributor (3); Intake pump (1), valve (2), water distributor (3) link to each other in order; The outer mixed-liquor return pump (15) that is provided with of anaerobic hydrolysis tower (5), aerobic device (8) bottom is provided with aerating system (9), and aerating system (9) links to each other with gas blower (7); Two sink devices (11) outlet at bottom links to each other with aerobic device (8) bottom through mud return line (13) through two heavy district's sludge reflux pumps (12), and two sink devices (11) top is provided with rising pipe (14).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201120503742 CN202499759U (en) | 2011-12-07 | 2011-12-07 | Anaerobic hydrolysis system for treating wastewater difficult to degrade biochemically |
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| Application Number | Priority Date | Filing Date | Title |
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| CN 201120503742 CN202499759U (en) | 2011-12-07 | 2011-12-07 | Anaerobic hydrolysis system for treating wastewater difficult to degrade biochemically |
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| CN202499759U true CN202499759U (en) | 2012-10-24 |
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Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102515426A (en) * | 2011-12-07 | 2012-06-27 | 浙江省环境保护科学设计研究院 | Anaerobic hydrolysis system for treating biorefractory waste water and anaerobic hydrolysis technology adopting the anaerobic hydrolysis system |
| CN104891653A (en) * | 2015-05-27 | 2015-09-09 | 福建洋屿环保科技股份有限公司 | Treatment method and treatment system for garbage leachate |
| CN114590960A (en) * | 2022-03-02 | 2022-06-07 | 杭州盛景环保工程有限公司 | Petrochemical wastewater treatment process system |
-
2011
- 2011-12-07 CN CN 201120503742 patent/CN202499759U/en not_active Expired - Fee Related
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102515426A (en) * | 2011-12-07 | 2012-06-27 | 浙江省环境保护科学设计研究院 | Anaerobic hydrolysis system for treating biorefractory waste water and anaerobic hydrolysis technology adopting the anaerobic hydrolysis system |
| CN104891653A (en) * | 2015-05-27 | 2015-09-09 | 福建洋屿环保科技股份有限公司 | Treatment method and treatment system for garbage leachate |
| CN104891653B (en) * | 2015-05-27 | 2018-06-01 | 福建洋屿环保科技股份有限公司 | The processing method and processing system of a kind of landfill leachate |
| CN114590960A (en) * | 2022-03-02 | 2022-06-07 | 杭州盛景环保工程有限公司 | Petrochemical wastewater treatment process system |
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| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20121024 Termination date: 20151207 |
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| EXPY | Termination of patent right or utility model |