CN202808482U - System for utilizing lateral bioreactor to carry out sludge reduction - Google Patents
System for utilizing lateral bioreactor to carry out sludge reduction Download PDFInfo
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- CN202808482U CN202808482U CN 201220462194 CN201220462194U CN202808482U CN 202808482 U CN202808482 U CN 202808482U CN 201220462194 CN201220462194 CN 201220462194 CN 201220462194 U CN201220462194 U CN 201220462194U CN 202808482 U CN202808482 U CN 202808482U
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Abstract
The utility model discloses a system for utilizing a lateral bioreactor to carry out sludge reduction. The system comprises an oxygen-free pool, an oxygenating pool and a solid-liquid separation pool which are connected in sequence, and further comprises the lateral bioreactor, wherein the lateral bioreactor is internally separated into a mixing region and an agitating and reacting region which are communicated with each other; the mixing region is communicated to the oxygen-free pool through a first water inlet pipe and the mixing region is communicated to the oxygenating pool through a second water inlet pipe; the agitating and mixing region is internally provided with an agitating device; and the bottom of the agitating and mixing region is communicated with the oxygenating pool through a mixed liquid reflowing pipe. According to the system disclosed by the utility model, a facultative environment and an oxygenating environment are utilized for carrying out alternative circulation treatment in an alternating manner, so that the system can continuously select low-breeding bacteria to be used for decomposing biological solids until the biological solids are completely decomposed; and the production amount of residual sludge is greatly reduced.
Description
Technical field
The utility model relates to technical field of sewage, is specifically related to a kind of mud decrement system that utilizes the side direction bio-reactor that double oxygen environment and oxygenation environment alternate cycles are processed.
Background technology
Widely used Wastewater Treated by Activated Sludge Process sewage, although technology maturation, a large amount of mud that produce in the treating processes, its excess sludge are processed and are usually accounted for 25%～65% of sewage work's overall running cost.
Excess sludge process to be disposed roughly following several feasible method: the one, carry out sanitary landfill after excess sludge reached related request, this kind disposal technology also is the most widely used method of present China, but the existence of the problems such as floor space is large, secondary pollution is serious has restricted the following prospect of the application of this method of disposal.The 2nd, burn after excess sludge reached related request, but the off gas treatment after burning is a unmanageable important difficult point, has also restricted the development of the method.The 3rd, excess sludge is fully utilized, perhaps excess sludge is made building material (or certain class low grade products) additive or gac etc.; Perhaps excess sludge is carried out agriculturally, increase soil fertility; Perhaps excess sludge is obtained the fuel byproduct by mud melting, pyrolytic decomposition and extract useful chemical substance etc. from excess sludge, but this type of comprehensive utilization is quite high to the relevant quality requirements of excess sludge, desired technology is also very high, domestic correlation technique does not also reach this level at present, and the development of method of comprehensive utilization also need further grope and study.The 4th, from sewage treatment process, reduce the generation of mud, being Sludge Pre-position Minimization, from the generation of source control excess sludge, is most economical method from the processing disposal options of mud, both reduced the sludge creation amount, the variety of problems of having avoided again subsequent disposal to bring.
The Sludge Pre-position Minimization technology can be divided into two large classes: physico-chemical processes and microorganism treatment.Physico-chemical processes mainly is to adopt molten born of the same parents' technology, and that utilizes physical method has heating, ultrasonic wave, a pressure etc.For example, application number is the Technology that 200510122935.8 Chinese patent literature discloses a kind of residual sludge reduction, this Technology is used for the sludge treatment flow process with sound field, reaches to promote sludge dewatering, anaerobic digestion, finally reaches the purpose of sludge reduction.
That utilizes chemical process has ozone oxidation, adds oxychlorination etc.For example, application number is that 201010121171.1 Chinese invention patent discloses a kind of method of utilizing ozone oxidation to realize reducing biological sludge, with A
2The biological treatment system of/O technique and ozone oxidation system combine, sewage is in the anaerobism section of biological treatment system, finish respectively anaerobic phosphorus release in anoxic section and the aerobic section, after the processes such as denitrification and aerobic suction phosphorus, excess sludge enters by ozonizer again, the ozone oxidation system that ozone contact post and device for absorbing tail gas three parts form, through ozone oxidation, the excess sludge cell wall structure is destroyed, excess sludge after the oxidation enters in the sewage biological treatment system with the form of organic matter, biological degradation by active sludge, its part organic matter transformation is become water and carbonic acid gas, thus the biological sludge amount that the reduction system produces.
Microorganism treatment mainly comprises increases the concentration of microorganism in reaction tank, such as membrane bioreactor (MBR), biological filter, prolongation aeration process, in the aerobe treatment system, utilize protozoon and metazoal predation, reduce mud amount and implement new technique; Utilize in addition microfauna to the predation of the microorganism in the biological treatment system and bacterium to reach the purpose of mud decrement.For example, application number is that 201110297195.7 Chinese invention patent application discloses a kind of utilize metazoan reinforcement sludge original position abatement system and technique and application.The present invention is made of anaerobic zone, oxygen-starved area, aerobic zone, metazoan vitellarium, two heavy districts, five parts, and biochemical system carries out the original position decrement by the metazoan vitellarium is set in the process of disposing of sewage; In the metazoan vitellarium, constantly add through the metazoan of cultivating domestication and strengthen the microorganism predation effect, realize the purpose of sludge in-situ decrement, can realize the mud decrement effect to active sludge 50-80%.
In the above-mentioned Sludge Reduction Technologies, its shortcoming is arranged respectively, the decrement effect of mud is limited, so Sludge Reduction Technologies is still waiting the further new technology of exploitation.
The utility model content
The utility model provides a kind of system that utilizes the side direction bio-reactor to carry out mud decrement, utilizes hold concurrently oxygen environment and the processing of oxygenation environment alternate cycles, makes system constantly select low breeding bacterium to come the decomposing organism solid.Until biosolids is decomposed the generation of greatly less excess sludge fully.
A kind of system that utilizes the side direction bio-reactor to carry out mud decrement, comprise the anaerobic tank, oxygenation pond and the solid-liquid separation tank that connect successively, also comprise a side direction bio-reactor, be separated into the mixing zone and the stirring reaction district that are interconnected in the described side direction bio-reactor, described mixing zone is communicated to described anaerobic tank by the first water inlet pipe, described mixing zone is communicated to described oxygenation pond by the second water inlet pipe, described mixing arranges whipping appts in the district, the described bottom, district that mixes is communicated with described oxygenation pond by the mixed-liquor return pipe.
System of the present utility model adopts Wastewater Treated by Activated Sludge Process sewage, pending sewage passes through anaerobic tank and oxygenation pond successively, in the oxygenation pond in the mud take the microorganism of aerobic repiration as main, organism in the sewage is resolved into micromolecular dissolved organic matter by the extracellular enzyme of microorganism, deliquescent organism enters the inherent oxygenation of microorganism cells pond and is degraded and transforms in sewage, part organic substance carries out katabolism, be oxidized to carbonic acid gas and water, and the synthetic required energy of new cell of acquisition, another part material carries out anabolism, form new cellular material, and in the mode of excess sludge finally by the solid-liquid separation tank removal system.
In order to reduce the quantity discharged of excess sludge, in the system of the present utility model, the first water inlet pipe extracts a part of anaerobic mixed solution to the side direction bio-reactor from anaerobic tank, the second water inlet pipe extracts a part of oxygenation mixed solution to the side direction bio-reactor from the oxygenation pond, the anaerobic mixed solution mixes the rear oxygen environment of holding concurrently that forms with the oxygenation mixed solution in the side direction bio-reactor, in the side direction bio-reactor, the oxygen bacterium of holding concurrently accounts for leading, holding concurrently, the oxygen bacterium is degraded respectively and residue and the byproduct of metabolism oxygenation bacterium, when reacted mixed solution turns back to the oxygenation pond, the oxygen bacterium of holding concurrently is decomposed by the oxygenation bacterium in the oxygenation pond again, by recycle system so, system constantly selects low breeding bacterium to come the decomposing organism solid, until biosolids is decomposed fully, greatly reducing the generation of excess sludge, mainly is to the oxygen environment of holding concurrently is provided in the side direction bio-reactor from the anaerobic mixed solution of anaerobic tank.
Side direction bio-reactor described in the utility model is the bio-reactor of a routine, be arranged on as bypass in the treatment system of activated sludge process, be arranged to mixing zone and stirring reaction district two lattice in the reactor, in the mixing zone, mix in the mixing zone from the anaerobic mixed solution of anaerobic tank with from the oxygenation mixed solution in oxygenation pond, in the stirring reaction district, after mixing, two strands of mixed solutions in the stirring reaction district, dominate the oxygen reaction of holding concurrently, preferably, the volume ratio in described mixing zone and stirring reaction district is 1: 3～5.
Preferably, be provided with mud return line between described solid-liquid separation tank and the described side direction bio-reactor, by this mud return line with the part sludge reflux in the solid-liquid separation tank to the side direction bio-reactor, described mud return line is connected to described mixing zone, with the sludge reflux in the solid-liquid separation tank to the mixing zone.
For the mixed solution in the side direction bio-reactor is transmitted back in the oxygenation pond more smoothly, preferably, described mixed-liquor return pipe is provided with the first pressure-feeding apparatus, and described the first pressure-feeding apparatus generally adopts the muddy water pump.
For the mud in the solid-liquid separation tank is back in the side direction bio-reactor smoothly, preferably, described mud return line is provided with the second pressure-feeding apparatus, and described the second pressure-feeding apparatus is generally selected sludge pump.
Preferably, described solid-liquid separation tank is for being second pond or sequencing batch reactor; Described second pond is rectangular sedimentation tank or inclined tube (plate) formula settling tank, and when selecting rectangular sedimentation tank, the mud in the settling tank is extracted out by vacuum pump, then is back in the side direction bio-reactor; When adopting inclined tube (plate) formula settling tank, the mud return line with pump directly is set in the settling tank bottom, be back to the side direction bio-reactor.
The beneficial effects of the utility model:
The utility model is to belong to the Sludge Pre-position Minimization technology, by research of the present utility model, can effectively reduce the sludge creation amount of system.Native system is the mixing reactor that utilizes a side direction, and with the liquid mixing of anaerobic device and oxygenate apparatus, the oxygen bacterium of holding concurrently in the side direction bio-reactor accounts for leading, and holding concurrently, the oxygen bacterium is degraded respectively and residue and the byproduct of metabolism oxygenation bacterium.When liquid turned back to oxygenate apparatus, the oxygen bacterium of holding concurrently was decomposed again.By recycle system so, system constantly selects low breeding bacterium to come the decomposing organism solid, until solid is decomposed fully, this will greatly reduce the generation of excess sludge.
Description of drawings
Fig. 1 is structural representation of the present utility model.
Embodiment
As shown in Figure 1, a kind of system that utilizes the side direction bio-reactor to carry out mud decrement, main body adopts conventional active sludge processing system, comprises the anaerobic tank 2, oxygenation pond 3 and the solid-liquid separation tank 12 that set gradually.
Anaerobic tank 2 adopts conventional anaerobic tank, and its sidewall is provided with water inlet pipe 1, is provided with water pipe between anaerobic tank 2 and the oxygenation pond 3; Conventional oxygenation pond is adopted in oxygenation pond 3,3 bottoms, oxygenation pond are provided with aerating apparatus 6, aerating apparatus 6 by some be tiled in the aeration tube at the bottom of 3 ponds, oxygenation pond and be the some solarization air caps that are distributed on the aeration tube form, the external apparatus of oxygen supply 5 of the supervisor of aeration tube, portion support device 5 can adopt gas blower.
Solid-liquid separation tank 12 adopts the ramp type settling tank, and oxygenation pond 3 is communicated to this ramp type settling tank by rising pipe 11, and clear water and mud after ramp type settling tank solid-liquid separation discharge respectively.
Comprise that also a setting position is than the equal low side direction bio-reactor 4 of anaerobic tank 2 and solid-liquid separation tank 3, side direction bio-reactor 4 internal mains will be divided into two lattice, wherein lattice are mixing zones, mainly be the mixed solution that receives from oxygenation pond 2 and anaerobic tank 3, it is mixed, other lattice are stirring reaction districts, play the leading reaction effect, setting device 17 in the stirring reaction district, and this whipping appts 17 adopts overhead stirrer, and the volume ratio in mixing zone and stirring reaction district is about 1: 3～and 5.
The mixing zone of this side direction bio-reactor 4 is communicated to anaerobic tank 2 by the first water inlet pipe 7, extracts in the part anaerobic tanks 2 the anaerobic mixed solution to the mixing zone of side direction bio-reactor 4 by the first water inlet pipe 7; The mixing zone of this side direction bio-reactor 4 also is communicated in the oxygenation pond 3 by the second water inlet pipe 8, extracts oxygenation mixed solution in the part oxygenation ponds 3 to side direction bio-reactor 4 mixing zones by the second water inlet pipe 8; The bottom in these side direction bio-reactor 4 stirring reaction districts is communicated in the oxygenation pond 3 by mixed-liquor return pipe 9.
At this mixed-liquor return pipe 9 the first pressure-feeding apparatus 10 is set, the first pressure-feeding apparatus 10 is selected the muddy water pump in the present embodiment, by this muddy water pump and mixed-liquor return pipe 9 with reacted mixed-liquor return in the side direction bio-reactor 4 to oxygenation pond 3; The liquid level absolute altitude of side direction bio-reactor 4 is lower than the liquid level absolute altitude in anaerobic tank 2 and oxygenation pond 3, and the mixed solution in the first water inlet pipe 7 and the second water inlet pipe 8 leans on the automatic inflow side of kinetic force of liquid level difference in bio-reactor 4, therefore need not the setting pressure e Foerderanlage.
The bottom of ramp type settling tank arranges mud return line 14, mud return line 14 is communicated to the bottom of side direction bio-reactor 4 mixing zones, at this mud return line 14 the second pressure-feeding apparatus 13 is set, this second pressure-feeding apparatus 13 is selected sludge pump in the present embodiment.
Ramp type settling tank top is provided with Graceful water pipe 16, connects excess sludge discharge pipe 15 at mud return line 14 by a threeway.
Be equipped with flowrate control valve on all pipelines.
Technical process of the present utility model is as follows:
When native system uses, sewage passes through first certain pre-treatment, comprises adjusting, just behind the treatment facility such as heavy, and sewage enters anaerobic tank 2 and the oxygenation pond 3 of native system successively, wherein oxygenation pond 3 provides dissolved oxygen in the sewage by apparatus of oxygen supply 5 and aerating apparatus 3, and Dissolved Oxygen concentration Control is at 2～4mg/L.
Simultaneously, anaerobic mixed solution in the anaerobic tank 2 carries a part (at every turn carry treatment sewage flow 10～30%) to the mixing zone of side direction bio-reactor 4 by the first water inlet pipe 7, the oxygenation mixed solution carries a part (at every turn carry treatment sewage flow 10～30%) to the mixing zone of side direction bio-reactor 4 by the second water inlet pipe 8 in the oxygenation pond 3, the volume ratio of each two strands of mixed solutions that extract is 1: 1, two strands of mixed solutions enter the stirring reaction district after the mixing zone mixes, starting whipping appts 17 reacts, mud return line 14 with the sludge reflux part in the solid-liquid separation tank 12 to side direction bio-reactor 4, abundant hybrid reaction certain hour in this side direction bio-reactor 4, the residence time is controlled at 2～4 hours, and then the mixed solution in the side direction bio-reactor 4 is delivered to oxygenation pond 3 by mixed-liquor return pipe 9.Like this alternate cycles, cycle index determine according to the solid pollution substrate concentration in the treatment sewage, until the biosolids mass degradation in the oxygenation pond 3 is complete, reaches the purpose of mud decrement.Then, the supernatant liquor in oxygenation pond 3 continues to flow to solid-liquid separation tank 12, solid-liquid separation tank 12 passes through mud-water separation, mud is back to the mixing zone of side direction bio-reactor 4 with the second pressure-feeding apparatus 13 parts, a part is discharged, and the supernatant liquor of solid-liquid separation tank 12 just discharges or enter next treatment unit.
In side direction bio-reactor 4, after mixing with the anaerobic mixed solution, the oxygenation mixed solution forms the oxygen environment of holding concurrently, the oxygen bacterium of holding concurrently is occupied an leading position, holding concurrently, the oxygen bacterium is degraded respectively and residue and the byproduct of metabolism oxygenation bacterium, when reacted mixed solution turns back to the oxygenation pond, the oxygen bacterium of holding concurrently is decomposed by the oxygenation bacterium in the oxygenation pond again, by recycle system so, system constantly selects low breeding bacterium to come the decomposing organism solid, until solid is decomposed fully, greatly reducing the generation of excess sludge, mainly is to the oxygen environment of holding concurrently is provided in the side direction bio-reactor from the anaerobic mixed solution of anaerobic tank.
Embodiment 1
Certain sewage plant does not carry out before mud decrement transforms at original treatment process, and excess sludge is about 2t/d (water ratio 80%) every day.The mud decrement transformation has increased a side direction bio-reactor at original treatment process, namely adopts system of the present utility model and technique, and excess sludge is about 0.5t/d (water ratio 80%) every day.Considerable change had not occured in effluent quality before and after the mud decrement transformation.
Embodiment 2
Certain newly-built sewage plant, according to the sewage water yield and the water quality situation of enterprise, former estimation excess sludge generating capacity is about 10t/d (water ratio 80%).Increase a side direction bio-reactor at sewage treatment process, namely adopt system of the present utility model and technique, after sewage plant built up steady running, the excess sludge generating capacity was about 2t/d (water ratio 80%).Effluent quality also can reach design requirements substantially.
The above only is better implementation example of the present utility model, is not limited to the utility model, and is all within the utility model spirit and principle, any modification of doing, is equal to replacement, improvement etc., all should be included within the protection domain of the present utility model.
Claims (6)
1. system that utilizes the side direction bio-reactor to carry out mud decrement, comprise the anaerobic tank (2) that connects successively, oxygenation pond (3) and solid-liquid separation tank (12), it is characterized in that, also comprise a side direction bio-reactor (4), be separated into the mixing zone and the stirring reaction district that are interconnected in the described side direction bio-reactor (4), described mixing zone is communicated to described anaerobic tank (2) by the first water inlet pipe (7), described mixing zone is communicated to described oxygenation pond (3) by the second water inlet pipe (8), described mixing arranges whipping appts (17) in the district, the described bottom, district that mixes is communicated with described oxygenation pond (3) by mixed-liquor return pipe (9).
2. system according to claim 1 is characterized in that, the volume ratio in described mixing zone and stirring reaction district is 1: 3～5.
3. system according to claim 2 is characterized in that, is provided with mud return line (14) between described solid-liquid separation tank (12) and the described side direction bio-reactor (4).
4. system according to claim 3 is characterized in that, described mixed-liquor return pipe (9) is provided with the first pressure-feeding apparatus (10).
5. system according to claim 4 is characterized in that, described mud return line (14) is provided with the second pressure-feeding apparatus (13).
6. system according to claim 5 is characterized in that, described solid-liquid separation tank (12) is second pond or sequencing batch reactor.
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| Application Number | Priority Date | Filing Date | Title |
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| CN 201220462194 CN202808482U (en) | 2012-09-12 | 2012-09-12 | System for utilizing lateral bioreactor to carry out sludge reduction |
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| CN 201220462194 CN202808482U (en) | 2012-09-12 | 2012-09-12 | System for utilizing lateral bioreactor to carry out sludge reduction |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102897912A (en) * | 2012-09-12 | 2013-01-30 | 浙江省环境保护科学设计研究院 | System and method for sludge reduction by using lateral bioreactor |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
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| CN102897912A (en) * | 2012-09-12 | 2013-01-30 | 浙江省环境保护科学设计研究院 | System and method for sludge reduction by using lateral bioreactor |
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| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20130320 Termination date: 20170912 |
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| CF01 | Termination of patent right due to non-payment of annual fee |