CN202829702U - Anaerobic system used for treating garbage dialysate - Google Patents
Anaerobic system used for treating garbage dialysate Download PDFInfo
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- CN202829702U CN202829702U CN2012204245057U CN201220424505U CN202829702U CN 202829702 U CN202829702 U CN 202829702U CN 2012204245057 U CN2012204245057 U CN 2012204245057U CN 201220424505 U CN201220424505 U CN 201220424505U CN 202829702 U CN202829702 U CN 202829702U
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E50/00—Technologies for the production of fuel of non-fossil origin
- Y02E50/30—Fuel from waste, e.g. synthetic alcohol or diesel
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Abstract
The utility model provides anaerobic system used for treating garbage dialysate and belongs to the field of the garbage treating device. The anaerobic system used for treating the garbage dialysate comprises a reactor, an insulating layer, a water inlet, a water outlet, a sludge discharging device, an end socket, a water distributor, a packing layer, a stirring device and a biogas guiding and discharging device, wherein the reactor is covered by the insulating layer, the water inlet is arranged on the lower portion of the reactor and the water outlet is arranged on the upper portion of the reactor. The end socket is arranged on the top of the reactor and the sludge discharging device is arranged at the bottom of the reactor. The water distributor is arranged on the lower portion inside the reactor and the water distributor is communicated with the water inlet. The reactor which is arranged between the water inlet and the water outlet is provided with the packing layer. The stirring device is arranged in the reactor. The biogas guiding and discharging device is arranged on the end socket. The anaerobic system used for treating the garbage dialysate is simple in structure and improves the efficiency of separating mud and water of the treated garbage dialysate and treatment effect through the cooperation of the packing layer, the stirring device and the water distributor.
Description
Technical field
The utility model relates to field of waste water treatment, particularly a kind of anaerobic system for the high-concentration garbage percolate processing.
Background technology
Trash processing way comprises sanitary landfill, burning, compost etc., but which kind of technique all can produce percolate.Current, refuse leachate treatment technology is still a global problem, wherein especially processes more difficult with high-concentration garbage percolate.For the higher garbage leachate of Pollutant levels, adopt anaerobic treatment can significantly remove pollutent, thereby reduce the volume of subsequent disposal structures, cost saving, reduction working cost.Current, anaerobic processing device adopts upflow anaerobic sludge blanket process more.
As shown in Figure 1, present upflow anaerobic sludge blanket process comprises a cylindrical reactor 1, the top of reactor 1 is provided with an end socket 2, be provided with percolate import 3 in the bottom of reactor 1, be provided with water outlet 4 on the top of reactor 1, be provided with mud discharging mouth 5 in the bottom of reactor 1, the mud that anaerobic treatment produces is discharged from mud discharging mouth 5.Because reactor design is not considered the character of mud, can encounter difficulties during spoil disposal, a large amount of mud occur and gathers, the phenomenon that can't discharge.Be provided with a biogas guide mouth 6 on the spherical shell cover 2 at the top of reactor 1, biogas is very not thorough with separating of percolate, and the biogas water ratio is very high, for the follow-up works such as biogas aqueous vapor shunting are made troubles.
The utility model content
The problems such as the purpose of the utility model embodiment provides a kind of anaerobic system for the percolate processing, can solve present upflow anaerobic sludge blanket process and exist operation water convenient, and efficient is low.This anaerobic system is simple to operate, stable, treatment effect is good, running cost is low.
The purpose of this utility model is achieved through the following technical solutions:
The utility model embodiment provides a kind of anaerobic system for the percolate processing, comprising:
Reactor, thermal insulation layer, water-in, water outlet, device for discharging sludge, end socket, water distributor, packing layer, whipping appts and biogas drainage device; Wherein,
Described reactor outside coats described thermal insulation layer, and reactor lower part is provided with water-in, and top is provided with water outlet;
Described reactor head arranges described end socket, and the bottom arranges described device for discharging sludge;
The bottom is provided with described water distributor in the described reactor, and water distributor is communicated with described water-in;
Described packing layer is set in the reactor between described water-in and the water outlet;
Described whipping appts is set in the described reactor;
Described biogas drainage device is arranged on the described end socket.
Can be found out by the above-mentioned technical scheme that provides, the anaerobic system that the utility model embodiment provides, simple in structure, cooperate by packing layer, whipping appts, water distributor, the mud, moisture that has improved the percolate of processing from efficient and treatment effect.
Description of drawings
In order to be illustrated more clearly in the technical scheme of the utility model embodiment, the accompanying drawing of required use was done to introduce simply during the below will describe embodiment, apparently, accompanying drawing in the following describes only is embodiment more of the present utility model, for those of ordinary skill in the art, under the prerequisite of not paying creative work, can also obtain other accompanying drawings according to these accompanying drawings.
The upflow anaerobic sludge blanket process synoptic diagram that Fig. 1 provides for prior art;
The anaerobic system synoptic diagram that Fig. 2 provides for the utility model embodiment;
Fig. 3 is the anaerobic system synoptic diagram that the interpolation side that provides of the utility model embodiment stirs.
Embodiment
Below in conjunction with the accompanying drawing among the utility model embodiment, the technical scheme among the utility model embodiment is clearly and completely described, obviously, described embodiment only is the utility model part embodiment, rather than whole embodiment.Based on embodiment of the present utility model, those of ordinary skills belong to protection domain of the present utility model not making the every other embodiment that obtains under the creative work prerequisite.
Below in conjunction with accompanying drawing the utility model embodiment is described in further detail.
The utility model embodiment provides a kind of anaerobic system for the percolate processing, as shown in Figure 2, this anaerobic system comprises: reactor 1, thermal insulation layer 3, water-in 6, water outlet 8, device for discharging sludge 5, end socket 9, water distributor 4, packing layer 7, whipping appts 2 and biogas drainage device 10;
Wherein, described reactor outside coats described thermal insulation layer, can be incubated whole equipment, and reactor lower part is provided with water-in, and top is provided with water outlet;
Described reactor head arranges described end socket, and the bottom arranges described device for discharging sludge;
The bottom is provided with described water distributor in the described reactor, and water distributor is communicated with described water-in;
Described packing layer is set in the reactor between described water-in and the water outlet;
Described whipping appts is set in the described reactor;
Described biogas drainage device is arranged on the described end socket.
In the above-mentioned anaerobic system, reactor is cylindrical or square column type, and reactor material can adopt steel or Steel Concrete etc.
In the above-mentioned anaerobic system, packing layer is multilayer, is disposed on from bottom to up in the reactor between described water-in and the water outlet.Generally according to the height of reactor, packing layer can be three layers, is disposed on from bottom to up in the reactor between described water-in and the water outlet, will be separated into a plurality of filter spaces in the reactor.Every layer of packing layer all adopts the protruded packing layer, is to consist of by cover the circular porous spherical particles thing of one deck at a skeleton, and the thickness of every layer of packing layer is that 1～3m(thickness can be decided according to organic pollutant content in the sewage).
In the above-mentioned anaerobic system, whipping appts is fixedly installed on the end socket, and the drive end of whipping appts is provided with agitating vane, and agitating vane is in the reactor of described packing layer top.If the multiple filling layers layer is arranged, then in the space reactor between every two-layer packing layer, one group of agitating vane is set all.
Device for discharging sludge 5 in the above-mentioned anaerobic system is conical hopper shape, and the unnecessary mud of generation is because the mixed settling region that is deposited in of gravity, and the device for discharging sludge 5 by conical hopper shape is beneficial to spoil disposal.
End socket in above-mentioned is conical head.
As shown in Figure 3, on the basis of above-mentioned anaerobic system, a plurality of whipping apptss 11 can also be set, each whipping appts 11 is installed on the reactor from the side, the agitating vane of each whipping appts is arranged in the reactor, be arranged on described water distributor and water distributor the top packing layer between the space in.
Below in conjunction with Fig. 2 above-mentioned anaerobic system is further described in detail:
In the anaerobic system of the utility model embodiment, reactor 1 bottom arranges water-in 6, and the water distributor 4 that is communicated with water-in 6 is arranged in the reactor 1, and percolate enters reactor 1 by water-in 6, evenly enters reactor 1 bottom through water distributor 4 again; Whipping appts 2 and packing layer 7 play the effects such as water distribution uniformity and dispersion flora, and water outlet 8 is on reactor 1 top, and the percolate after the processing is flowed out by water outlet 8; The device for discharging sludge 5 that is arranged on reactor 1 bottom is conical hopper shape, is conducive to collection and the discharging of mud; Biogas drainage device 10 is for vertically being arranged on the end socket 9, and the end socket of biogas drainage device 10 bottoms 9 is beneficial to collecting methane and discharging for inverted conical hopper shape; Thermal insulation layer 3 is thoroughly protected whole reactor 1, has the effects such as insulation, protection.
In the anaerobic system of the utility model embodiment, in reactor 1, establish the packing layer 7 of porous, every layer of packing layer 7 is to cover the circular porous spherical particles thing of one deck at a skeleton, and porous spherical particles has huge surface-area, and porous surface provides growing carrier for anaerobe; Anaerobic bacteria flora has generated one deck anaerobe film at filler, namely at reactor 1 interior formation anaerobe bed, is made by porous material because of packing layer 7, and the anaerobe film of formation also has huge surface.The thickness of every layer of packing layer is (thickness of every layer of packing layer also can be decided according to organic pollutant content in the sewage) between 1～3m.
The protruded packing layer 7 of establishing in the reactor 1 of above-mentioned anaerobic system has following effect:
(1) packing layer 7 provides carrier for anaerobe group's growth, anaerobic bacteria flora generates one deck anaerobe film at packing layer 7, namely at reactor 1 interior formation anaerobe bed, made by porous material because of packing layer 7, the anaerobe film of formation also has huge surface.When sewage passes through, increased the chance that organic pollutants contacts with the anaerobe film, so that anaerobic reaction is more abundant, the clearance of organic pollutant is higher.
(2) anaerobe is attached on the packing layer 7 with biomembranous form, thereby has reduced the anaerobic sludge in the sewage.Anaerobic treatment of the prior art is not high because of the separation efficiency of mud, water, and the sludge stream vector is more.Reactor 1 has increased after the packing layer, and reactor 1 interior anaerobe reservation amount is improved.The mud that anaerobic treatment produces mainly is the mud that comes off from packing layer 7, these mud that come off from packing layer 7 are under action of gravitation, be deposited to reactor 1 bottom downwards, discharged by the device for discharging sludge 5 that is arranged on reactor 1 bottom, this just greatly improved mud in the reactor, moisture from efficient.
The device for discharging sludge 5 that the utility model arranges in reactor 1 bottom is conical hopper shape, and the unnecessary mud that produces like this is because gravity can be conveniently through 5 discharges of conical hopper shape device for discharging sludge.Device for discharging sludge 5 has following effect:
(1) moisture percentage in sewage sludge is low, and sludge volume can drop to minimum, because conical hopper bottom is less, and is not subjected to water currents away from whipping appts, institute's mud that produces is in " static " state in device for discharging sludge 5 bottoms, moisture percentage in sewage sludge reduction, sludge volume reduction;
(2) mud homogeneous is beneficial to follow-up sludge dewatering treatment, is in mud " static " state so that the Sludge Property stable homogeneous that precipitates;
(3) spoil disposal is thorough, avoids dirty stifled.Under the conical hopper state, mud emits successively, the situation that can not cause peripheral mud to discharge.The mud homogeneous, discharging is stable, causes dirty stifled probability extremely low.
The anaerobic system of the utility model embodiment can adopt the anaeration in normal temperature reaction, generally can adopt 27 ℃～37 ℃ anaeration in normal temperature reaction, the most reasonable from technology and economic aspect, the technical process that utilizes anaerobic system that the utility model embodiment provides that percolate is processed is as follows:
(1) sewage flow process: percolate is sent in the reactor 1 from the water-in 6 of reactor 1 bottom by sump pump, behind water distributor 4 water distribution uniformities, through packing layer 7 and whipping appts 2, rises to water outlet 8 and discharges, and enters next treatment process;
(2) mud flow process: the mud (mainly being the mud that comes off by on the packing layer 7) that reactor 1 interior anaerobic treatment produces is collected by the device for discharging sludge 5 that is located at reactor 1 bottom conical hopper shape, regularly discharges;
(3) biogas flow process: the gases such as biogas that reactor 1 interior anaerobe produces in digestion organic pollutant process, overflow from liquid level, discharge through the biogas drainage device 10 that is arranged on the conical head 9.
The above; it only is the better embodiment of the utility model; but protection domain of the present utility model is not limited to this; anyly be familiar with those skilled in the art in the technical scope that the utility model discloses; the variation that can expect easily or replacement all should be encompassed within the protection domain of the present utility model.Therefore, protection domain of the present utility model should be as the criterion with the protection domain of claims.
Claims (9)
1. one kind is used for the anaerobic system that percolate is processed, and it is characterized in that, comprising:
Reactor, thermal insulation layer, water-in, water outlet, device for discharging sludge, end socket, water distributor, packing layer, whipping appts and biogas drainage device; Wherein,
Described reactor outside coats described thermal insulation layer, and reactor lower part is provided with water-in, and top is provided with water outlet;
Described reactor head arranges described end socket, and the bottom arranges described device for discharging sludge;
The bottom is provided with described water distributor in the described reactor, and water distributor is communicated with described water-in;
Described packing layer is set in the reactor between described water-in and the water outlet;
Described whipping appts is set in the described reactor;
Described biogas drainage device is arranged on the described end socket.
2. anaerobic system according to claim 1 is characterized in that, described reactor is cylindrical or square column type.
3. anaerobic system according to claim 1 is characterized in that, described packing layer is multilayer, is disposed on from bottom to up in the reactor between described water-in and the water outlet.
4. anaerobic system according to claim 3 is characterized in that, described packing layer is three layers, is disposed on from bottom to up in the reactor between described water-in and the water outlet, will be separated into a plurality of filter spaces in the reactor.
5. according to claim 1,3 or 4 described anaerobic systems, it is characterized in that described every layer of packing layer is to consist of by cover the circular porous spherical particles thing of one deck at a skeleton, the thickness of every layer of packing layer is 1～3m.
6. anaerobic system according to claim 1 is characterized in that, described whipping appts is fixedly installed on the end socket, and the drive end of whipping appts is provided with agitating vane, and agitating vane is in the described reactor of described packing layer top.
7. anaerobic system according to claim 1 is characterized in that, described end socket is conical head.
8. anaerobic system according to claim 1, it is characterized in that, also comprise: a plurality of whipping apptss, each whipping appts is installed on the described reactor from the side, the agitating vane of each whipping appts is arranged in the reactor, be arranged on described water distributor and water distributor the top packing layer between the space in.
9. anaerobic system according to claim 1 is characterized in that, described device for discharging sludge is conical hopper shape.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
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| CN2012204245057U CN202829702U (en) | 2012-08-24 | 2012-08-24 | Anaerobic system used for treating garbage dialysate |
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| Application Number | Priority Date | Filing Date | Title |
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| CN2012204245057U CN202829702U (en) | 2012-08-24 | 2012-08-24 | Anaerobic system used for treating garbage dialysate |
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| CN2012204245057U Expired - Fee Related CN202829702U (en) | 2012-08-24 | 2012-08-24 | Anaerobic system used for treating garbage dialysate |
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Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103613192A (en) * | 2013-12-19 | 2014-03-05 | 自贡大业高压容器有限责任公司 | Organic anaerobic reactor |
| CN106186305A (en) * | 2016-08-25 | 2016-12-07 | 广西壮族自治区环境保护科学研究院 | A kind of anaerobism carrier biofilm waste water treatment reactor |
| CN106809951A (en) * | 2015-11-27 | 2017-06-09 | 江苏启创环境科技有限公司 | Town domestic sewage dephosphorization apparatus |
| CN110272121A (en) * | 2019-07-01 | 2019-09-24 | 台州市永丰纸业有限公司 | A kind of anerobic sowage reactor |
| CN115818855A (en) * | 2023-02-02 | 2023-03-21 | 盐城工学院 | Solar energy circulation aeration suspension type biological filter |
| CN116102165A (en) * | 2022-12-07 | 2023-05-12 | 连云港赣榆康恒环保能源有限公司 | Leachate treatment system and method for garbage power plant |
-
2012
- 2012-08-24 CN CN2012204245057U patent/CN202829702U/en not_active Expired - Fee Related
Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103613192A (en) * | 2013-12-19 | 2014-03-05 | 自贡大业高压容器有限责任公司 | Organic anaerobic reactor |
| CN106809951A (en) * | 2015-11-27 | 2017-06-09 | 江苏启创环境科技有限公司 | Town domestic sewage dephosphorization apparatus |
| CN106186305A (en) * | 2016-08-25 | 2016-12-07 | 广西壮族自治区环境保护科学研究院 | A kind of anaerobism carrier biofilm waste water treatment reactor |
| CN110272121A (en) * | 2019-07-01 | 2019-09-24 | 台州市永丰纸业有限公司 | A kind of anerobic sowage reactor |
| CN116102165A (en) * | 2022-12-07 | 2023-05-12 | 连云港赣榆康恒环保能源有限公司 | Leachate treatment system and method for garbage power plant |
| CN115818855A (en) * | 2023-02-02 | 2023-03-21 | 盐城工学院 | Solar energy circulation aeration suspension type biological filter |
| CN115818855B (en) * | 2023-02-02 | 2023-08-15 | 盐城工学院 | Solar circulation aeration suspension type biological filter |
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| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20130327 Termination date: 20190824 |
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| CF01 | Termination of patent right due to non-payment of annual fee |