CN201148379Y - Anaerobic reaction tower water distributor - Google Patents
Anaerobic reaction tower water distributor Download PDFInfo
- Publication number
- CN201148379Y CN201148379Y CNU2007201910620U CN200720191062U CN201148379Y CN 201148379 Y CN201148379 Y CN 201148379Y CN U2007201910620 U CNU2007201910620 U CN U2007201910620U CN 200720191062 U CN200720191062 U CN 200720191062U CN 201148379 Y CN201148379 Y CN 201148379Y
- Authority
- CN
- China
- Prior art keywords
- reaction tower
- anaerobic reaction
- flow guiding
- guiding disc
- water
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Lifetime
Links
Images
Classifications
-
- Y02W10/12—
Abstract
The utility model discloses a water distribution device of an anaerobic reaction tower. The anaerobic reaction tower is provided with a plurality of flow guide plates with gradually decreasing diameters from the outside to the inside of the tower; the flow guide plates are fixed on the bottom plate by a fixing frame, and are provided with a plurality of plate-surface injectors with the water flow of the same clockwise or counterclockwise direction. The water distribution device can fully mix the water, mud (biological phase) and air in the radial direction and the axial direction. And the water distribution device has the advantages of no generation of dead angles, smooth interval channels, dynamic balance, simple structure, and convenient manufacture.
Description
Technical field
The utility model relates to wastewater treatment equipment, particularly relates to a kind of anaerobic reaction tower water distributor.
Background technology
The waste water of Organic pollutants will carry out wastewater treatment, is up to state standards, and just can be discharged into river, lake, river, sea.Method of wastewater treatment is a lot, but present home and abroad in the art, and first road treatment process mainly is an anaerobic biochemical, and its processing unit equipment claims " anaerobic biochemical reactor (tower) ".
The wastewater treatment anaerobic biochemical reactor also has a lot of inside and outside members except that tower body, and wherein the internals of most critical is a water water-distributing device into.The requirement of water inlet water distribution: Yuan Shui will fully contact with the interior anaerobism water of tower, mix closely, with reach in time, the purpose of homogenizing mass transfer, heat transfer, the more important thing is simultaneously will be by the advanced person the water inlet water-distributing device microorganism of active particle mud contacted fully with organic pollutant in the anaerobism water and mix to reach, and the generation biochemical reaction, to bring into play the treatment efficiency of reactor to greatest extent.The different internal structure function of anaerobic biochemical reactor can form the flow state of different inside anaerobism water, biological bed.The anaerobic biochemical wastewater treatment has the anaerobic reaction tower of a lot of style structures, and wherein most crucial member is a water water distributor into.Present water inlet water distributor both domestic and external exists the problem of ubiquity to be: layout a lot and the water distribution inequality exists at " dead angle "; Because the water distribution inequality causes water, mud (biological bacteria), the mixing of gas three-phase, loose contact; Mass-and heat-transfer is homogenizing not, thereby causes local biochemical reaction excessive, causes acidifying, has changed the materialization controlled variable of reaction zone; Other has the considerable part cross section " to leave unused ", can not bring into play the maximum efficiency of bio-reactor; The anaerobic biological processing efficiency is poor, and load level is low; The anaerobism tower that past is conventional, because the anaerobism water that inner water distributor forms, biological bed fluidised form all are " upflow anaerobic sludge blanket reactors ", this reactor has two big shortcomings: as shown in Figure 1, current attitude straight line upwards, current are vertically upward to the reactive force of granule sludge, make mud rise liter easily, cause water outlet to float mud; Because the current straight line upwards, makes the water body flow path the shortest, be unfavorable for biochemical efficiency simultaneously.
The utility model content
The purpose of this utility model is to allow the intravital water of whole anaerobic biochemical reaction tower, mud (biological bacteria), gas three-phase mix fully, comprehensive engagement, realizes the average rate homogenizing, reaches the complete equilibrium state of mass-and heat-transfer.
For achieving the above object, the technical solution of the utility model provides a kind of anaerobic reaction tower water distributor, the coaxial arrangement flow guiding disc that has several diameters to reduce successively from outside to inside in the anaerobic reaction tower, described flow guiding disc is fixed on by fixed support on the base plate of described anaerobic reaction tower, and described flow guiding disc is provided with several water outlet directions and is all clockwise or counterclockwise card injector.
Wherein, also be provided with several water outlet directions tower base plate injector identical on the base plate of described anaerobic reaction tower with described card injector water outlet direction.
Wherein, described flow guiding disc is round table-like disk-shaped structure.
Wherein, described flow guiding disc try to get to the heart of a matter and the tower base plate of described anaerobic reaction tower between leave the fluid channel.
Wherein, described injector comprises enlarged tube, trunnion, negative pressure pipe and the water inlet pipe that connects successively, and described water inlet pipe is connected with the spray tube that extend in the described negative pressure pipe.
Wherein, described injector comprises the anchor that is used for fixing water inlet pipe with the negative pressure pipe coupling.
Wherein, described enlarged tube is the rectangle enlarged tube, and described rectangle enlarged tube osculum end is connected with described trunnion.
Wherein, the rectangle enlarged tube of described card injector is installed in described flow guiding disc upside, and described trunnion, negative pressure pipe and water inlet pipe are installed in described flow guiding disc downside.
Above-mentioned utility model technical scheme only is an optimal technical scheme of the present utility model, have following advantage: anaerobic reaction tower water distributor described in the utility model can make radially, axial water, mud (biophase), gas three-phase thorough mixing in reaction tower, spiral rises, there is not the dead angle fully, runner is unimpeded, running balance, and simple in structure, easily manufactured.
Description of drawings
Fig. 1 is the interior water distribution fluidised form synoptic diagram of a kind of anaerobic reaction tower of prior art;
Fig. 2 is the cross-sectional view of a kind of anaerobic reaction tower water distributor of the utility model embodiment;
Fig. 3 is the plan structure synoptic diagram of a kind of anaerobic reaction tower water distributor of the utility model embodiment;
Fig. 4 is the cross-sectional view of a kind of anaerobic reaction tower water distributor flow guiding disc of the utility model embodiment;
Fig. 5 is the plan structure synoptic diagram of a kind of anaerobic reaction tower water distributor flow guiding disc anchor of the utility model embodiment;
Fig. 6 is the structural representation of a kind of anaerobic reaction tower water distributor injector of the utility model embodiment;
Fig. 7 is the interior water distribution rising fluidised form synoptic diagram of a kind of anaerobic reaction tower of the utility model embodiment.
Wherein, 1: tower base plate injector; 2: flow guiding disc; 3: tower body; 4: the tower base plate; 5: the card injector; 6: fixed support; 7: the rectangle enlarged tube; 8: trunnion; 9: the negative pressure pipe; 10: spray tube; 11: anchor; 12: water inlet pipe; 13: rectangular jet; 14: former current; 15: muddy water stream; 16: mixed flow.
Embodiment
Below in conjunction with drawings and Examples, embodiment of the present utility model is further described.Following examples only are used for the technical solution of the utility model more clearly is described, and can not limit protection domain of the present utility model with this.
As Fig. 2, shown in Figure 3, the anaerobic reaction tower water distributor of present embodiment includes the flow guiding disc 2 that three diameters reduce successively from outside to inside successively in anaerobic reaction Tata body 3, be respectively flow guiding disc A, B, C.According to the difference of tower body 3 diameters, more or less flow guiding disc 2 can be set, and be not only to be confined to three.Each flow guiding disc 2 is provided with the identical card injector 5 of a plurality of water outlet directions, the identical water export direction of each card injector 5 that is meant of water outlet direction is all clockwise or is all counterclockwise, flow guiding disc 2 diameters are big more, the card injector 5 that is provided with is also just many more, and usually, a plurality of card injectors 5 are arranged on the radial centre lines of flow guiding disc 2, i.e. uniform distribution on the circumference of flow guiding disc 2 preferably, for example, when 4 injectors 5 are set, injector 5 is set to 90 degree layouts at interval.The central axes of the central axis of a plurality of flow guiding discs 2 and anaerobic reaction tower.Tower base plate 4 is provided with tower base plate injector 1.Wherein, the water outlet direction of tower base plate injector 1 is identical with the water export direction of card injector 5.
Fig. 4 is the structural representation of a kind of anaerobic reaction tower water distributor flow guiding disc of the utility model embodiment, and Fig. 5 is the installation plan structure synoptic diagram of a kind of anaerobic reaction tower water distributor flow guiding disc of the utility model embodiment.Flow guiding disc 2 is installed on the tower base plate 4 by fixed support 6, and flow guiding disc 2 is round table-like disk-shaped structure, and big mouthful is Pan Kou, and osculum, is tried to get to the heart of a matter downwards when flow guiding disc 2 is installed for trying to get to the heart of a matter, and is that the tower mouth is last down here at the bottom of the tower that is meant the anaerobic reaction tower up and down of indication.Flow guiding disc 2 try to get to the heart of a matter and tower base plate 4 between leave the gap (the X mark among Fig. 4) of certain distance, as the fluid channel.Certain inclination angle (a mark among Fig. 4) is arranged on the flow guiding disc, guarantee water, mud (biophase), gas three-phase thorough mixing, the size at concrete inclination angle can be adjusted according to the height and the diameter of flow guiding disc, belongs to how much categories of mathematics, no longer describes in detail.
Fig. 6 is the structural representation of a kind of anaerobic reaction tower water distributor injector of the utility model embodiment.The injector here is meant card injector 5 and tower base plate injector 1.Injector comprises rectangle enlarged tube 7, trunnion 8, negative pressure pipe 9 and the anchor 11 that connects successively, and is fixed on the water inlet pipe 12 on the anchor 11, and water inlet pipe 12 is connected with the spray tube 10 that extend in the negative pressure pipe 9.The osculum end of rectangle enlarged tube 7 is connected with trunnion, it is to be noted that here enlarged tube must be the rectangle enlarged tube, is connected fully with trunnion, to change the current attitude, makes it plane injection on flow guiding disc.Former current 14 enter injector by water inlet pipe 12, and muddy water stream 15 enters into injector from negative pressure pipe 9, and former current 14 and muddy water stream 15 thorough mixing negative pressure pipe 9 and trunnion 8 in form mixed flow 16 and spray from the rectangular jet 13 of rectangle enlarged tube 7.When card injector 5 is installed on the flow guiding disc 2, the horizontal installation site of the horizontal installation site of the rectangle enlarged tube 7 of card injector 5 and trunnion 8, negative pressure pipe 9 and water inlet pipe 12 is positioned at card both sides up and down, level is meant parallel with tower base plate 4, that is to say that mixed flow 16 is to spray obliquely from card injector 5.After mixed flow 16 ejection, form " dynamically " continuously, because be all clockwise or counterclockwise injection direction, thus form centrifugal force, because centrifugal force, fluidised form radially, axial fluidised form synchronous operation.Serve as theme with radially big fluidised form, have simultaneously axially to have cross-flow of one's own, finally become spiral escalation, as shown in Figure 7.
The anaerobic reaction tower water distributor of present embodiment can be guaranteed whole tower body cross section synchronous dynamic, average rate homogenizing, reaches the complete equilibrium state of mass-and heat-transfer, does not have the dead angle.Thereby eliminate pollutent, the biophasic concentration gradient of biochemical zone, eliminate local reaction fully, restrain the pass key control of anaerobic biochemical reaction---acidifying phenomenon effectively.Former water, anaerobism water, granule sludge thorough mixing, the cloth pool can reach the boiling attitude.Guarantee that the three-phase fluidised form is uninterrupted, do not remain in a standstill, stablize and the expanded state that makes progress.The cloth pool of boiling attitude helps being delivered to whole reaction zone down, forms the bulking sludge bed, realizes high loading, high efficiency anaerobic biological tower.And water distribution mouth can not stop up, and forms three-phase " three mixed flow attitudes ", i.e. injector import and export itself are to mix for the first time; The injector outlet is owing to the impact of current, and the effect of multiple spot direction unanimity makes whole solution axially mix for the second time along tower body.By the centrifugal force of jet water course, be that matrix produces radially mixing for the third time of tower body with the flow guiding disc.Significant prolongation the flow paths of current in reactor.Simultaneously, make granule sludge to radially motion, but not motion is vertically upward floated the mud phenomenon so can reduce water outlet because current have action of centrifugal force to the reactive force of granule sludge.Simultaneously can help taking to strengthen separately the fluidised form of spiral attitude, more help the raising of volumetric loading and processing efficiency.
The above only is a preferred implementation of the present utility model; should be understood that; for those skilled in the art; under the prerequisite that does not break away from the utility model know-why; can also make some improvements and modifications, these improvements and modifications also should be considered as protection domain of the present utility model.
Claims (8)
1, a kind of anaerobic reaction tower water distributor, it is characterized in that, the coaxial arrangement flow guiding disc that has several diameters to reduce successively from outside to inside in the anaerobic reaction tower, described flow guiding disc is fixed on by fixed support on the base plate of described anaerobic reaction tower, and described flow guiding disc is provided with several water outlet directions and is all clockwise or counterclockwise card injector.
2, anaerobic reaction tower water distributor as claimed in claim 1 is characterized in that, also is provided with several water outlet directions tower base plate injector identical with described card injector water outlet direction on the base plate of described anaerobic reaction tower.
3, anaerobic reaction tower water distributor as claimed in claim 2 is characterized in that, described flow guiding disc is round table-like disk-shaped structure.
4, anaerobic reaction tower water distributor as claimed in claim 3 is characterized in that, described flow guiding disc try to get to the heart of a matter and the tower base plate of described anaerobic reaction tower between leave the fluid channel.
5, anaerobic reaction tower water distributor as claimed in claim 1 or 2 is characterized in that, described injector comprises enlarged tube, trunnion, negative pressure pipe and the water inlet pipe that connects successively, and described water inlet pipe is connected with the spray tube that extend in the described negative pressure pipe.
6, anaerobic reaction tower water distributor as claimed in claim 5 is characterized in that, described injector also comprises the anchor that is used for fixing water inlet pipe with the negative pressure pipe coupling.
7, anaerobic reaction tower water distributor as claimed in claim 6 is characterized in that, described enlarged tube is the rectangle enlarged tube, and described rectangle enlarged tube osculum end is connected with described trunnion.
8, anaerobic reaction tower water distributor as claimed in claim 7 is characterized in that, the rectangle enlarged tube of described card injector is installed in described flow guiding disc upside, and described trunnion, negative pressure pipe and water inlet pipe are installed in described flow guiding disc downside.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNU2007201910620U CN201148379Y (en) | 2007-12-29 | 2007-12-29 | Anaerobic reaction tower water distributor |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNU2007201910620U CN201148379Y (en) | 2007-12-29 | 2007-12-29 | Anaerobic reaction tower water distributor |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN201148379Y true CN201148379Y (en) | 2008-11-12 |
Family
ID=40116146
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CNU2007201910620U Expired - Lifetime CN201148379Y (en) | 2007-12-29 | 2007-12-29 | Anaerobic reaction tower water distributor |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN201148379Y (en) |
Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101585600B (en) * | 2009-06-15 | 2011-04-13 | 中国市政工程中南设计研究总院 | Moderate temperature UASB reactor water distribution device in diameter of more than 15 meter |
| CN102897911A (en) * | 2012-11-05 | 2013-01-30 | 广西金源生物化工实业有限公司 | Anaerobic tank jet-flow water distributor and water distribution blending system |
| CN104828940A (en) * | 2015-05-06 | 2015-08-12 | 褚保玉 | Anaerobic digestion method |
| CN105757857A (en) * | 2016-04-15 | 2016-07-13 | 重庆房地产职业学院 | Domestic evaporative cooling air conditioner with pulse electromagnetic valve |
| CN105757856A (en) * | 2016-04-15 | 2016-07-13 | 重庆房地产职业学院 | Domestic evaporative cooling air conditioner with electric control valve |
| CN105864929A (en) * | 2016-04-15 | 2016-08-17 | 重庆房地产职业学院 | Household evaporative cooling type air conditioner |
| CN107892387A (en) * | 2017-12-30 | 2018-04-10 | 珠海信环环保有限公司 | A kind of anaerobic jar water-distributing device for having both spoil disposal function |
-
2007
- 2007-12-29 CN CNU2007201910620U patent/CN201148379Y/en not_active Expired - Lifetime
Cited By (11)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101585600B (en) * | 2009-06-15 | 2011-04-13 | 中国市政工程中南设计研究总院 | Moderate temperature UASB reactor water distribution device in diameter of more than 15 meter |
| CN102897911A (en) * | 2012-11-05 | 2013-01-30 | 广西金源生物化工实业有限公司 | Anaerobic tank jet-flow water distributor and water distribution blending system |
| CN102897911B (en) * | 2012-11-05 | 2014-04-02 | 广西金源生物化工实业有限公司 | Anaerobic tank jet-flow water distributor and water distribution blending system |
| CN104828940A (en) * | 2015-05-06 | 2015-08-12 | 褚保玉 | Anaerobic digestion method |
| CN105757857A (en) * | 2016-04-15 | 2016-07-13 | 重庆房地产职业学院 | Domestic evaporative cooling air conditioner with pulse electromagnetic valve |
| CN105757856A (en) * | 2016-04-15 | 2016-07-13 | 重庆房地产职业学院 | Domestic evaporative cooling air conditioner with electric control valve |
| CN105864929A (en) * | 2016-04-15 | 2016-08-17 | 重庆房地产职业学院 | Household evaporative cooling type air conditioner |
| CN105864929B (en) * | 2016-04-15 | 2018-11-02 | 重庆房地产职业学院 | A kind of household evaporative air conditioning system |
| CN105757857B (en) * | 2016-04-15 | 2018-11-02 | 重庆房地产职业学院 | A kind of household evaporative air conditioning system with impulse electromagnetic valve |
| CN105757856B (en) * | 2016-04-15 | 2018-11-02 | 重庆房地产职业学院 | A kind of household evaporative air conditioning system with electric control valve |
| CN107892387A (en) * | 2017-12-30 | 2018-04-10 | 珠海信环环保有限公司 | A kind of anaerobic jar water-distributing device for having both spoil disposal function |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN201148379Y (en) | Anaerobic reaction tower water distributor | |
| CN201952281U (en) | Cyclone type waste water treatment device of swell anaerobic sludge bed | |
| CN1986453A (en) | UASB biological pneumatic circulation stirring technique | |
| CN101817586A (en) | Spiral-flow water-distribution hydrocyclone internal-circulation anaerobic reactor | |
| CN104085986B (en) | A kind of external loop airlift vortex enhanced biological nitrogen removal reactor | |
| CN203999136U (en) | External loop airlift vortex enhanced biological nitrogen removal reactor | |
| CN201362614Y (en) | Internal circulation anaerobic reactor for cyclone water distribution cyclone separation | |
| CN210736319U (en) | Spiral-flow type anaerobic reactor | |
| CN204752323U (en) | Vertical integrative sewage treatment device | |
| CN204097184U (en) | Integration is without gradient active sewage sludge treatment device | |
| CN203346172U (en) | Multi-zone bioreactor | |
| CN2741973Y (en) | High efficiency combined water distributor | |
| CN214734784U (en) | Internal circulation aerobic biological fluidized bed | |
| CN2574771Y (en) | Shower bath spring nozzle device | |
| CN211367123U (en) | Novel anaerobic biochemical circulation flow reactor | |
| CN210885507U (en) | Anaerobic reaction device with small-flux gas supply circulation stirring | |
| CN209778442U (en) | vortex reaction water distribution device | |
| CN211394017U (en) | Water distribution equipment of IC anaerobic reactor | |
| CN210559617U (en) | Rotary mixing type aeration device | |
| CN204138421U (en) | Be applied to the mixed-liquor return system of vertical AAO technique | |
| CN102351333A (en) | Turbulent flow mixed aerator | |
| CN202576074U (en) | Plug flow type internal circulating three phase bio-fluidized bed | |
| CN207016569U (en) | A kind of mushroom head for being used to fluidize cyclic aeration device | |
| CN207313222U (en) | A kind of intermittent aerating circular form biochemical reactor | |
| CN207016545U (en) | A kind of flow deflector for being used to fluidize cyclic aeration device |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CX01 | Expiry of patent term | ||
| CX01 | Expiry of patent term |
Granted publication date: 20081112 |