CN209481287U - A kind of standardization dimensional structure of more case anaerobic organism contact deflector reactors - Google Patents
A kind of standardization dimensional structure of more case anaerobic organism contact deflector reactors Download PDFInfo
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- CN209481287U CN209481287U CN201822012207.7U CN201822012207U CN209481287U CN 209481287 U CN209481287 U CN 209481287U CN 201822012207 U CN201822012207 U CN 201822012207U CN 209481287 U CN209481287 U CN 209481287U
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Abstract
The utility model discloses a kind of standardization dimensional structures of multiphase anaerobic organism contact deflector reactor, comprising: the first reaction chamber, the second reaction chamber, third reaction chamber, the 4th reaction chamber, vertical baffle plate, inclined baffle, filler, overflow port, water outlet, reaction frame；Sewage passes sequentially through overflow port when use, successively passes through the first reaction chamber, the second reaction chamber, third reaction chamber, the 4th reaction chamber, for the control of reaction room temperature at 25~35 DEG C, hydraulic detention time is 36~72 hours；4th reaction chamber be equipped with reflux water pump, by the 4th reaction chamber water and microorganism flow back into the first reaction chamber；The Institute of Micro-biology that sewage is adhered on filler in each reaction chamber decomposes, and the gas after decomposition directly passes through discharge above each reaction chamber, and the sewage after being disposed can enter next processing links by water outlet；The beneficial effects of the utility model are: improving biochemical efficiency, normalization is improved.
Description
Technical field
The utility model relates to arrive biochemistry, the standardization of specifically a kind of more case anaerobic organism contact deflector reactors
Dimensional structure.
Background technique
Anaerobic baffled reactor is a kind of new and effective anaerobic biological treatment apparatus, because of its special structure, with it
Its Anaerobic treatment technique is compared, and is had many advantages, such as movement-less part, low without mechanical mixture, Construction and operation expense
Deng；But current anaerobic baffled reactor is there is also some disadvantages, due to water flow do in the reactor above and below stream movement,
The upper and lower part of baffle certainly exists turbulent motion and the dead angle of liquid, so uniform water distribution is more tired for reactor
Difficulty is difficult to keep stable plug-flow state in single reaction chamber；And in practical projects, key parameter still relies upon engineering warp
It tests；The utility model proposes a kind of design parameters of novel multi-phase anaerobic baffled reactor, to its structure type, part dimension etc.
New data mode is provided, can effectively solve the problems, such as that uniform conventional anaerobic baffled reactor exists.
Utility model content
The purpose of this utility model is to provide a kind of standardization size knots of more case anaerobic organism contact deflector reactors
Structure provides intuitive ratio data shape with structure type, the part dimension etc. to more case anaerobic organism contact deflector reactors
Formula makes the inside of more case anaerobic organism contact deflector reactors keep stable plug-flow state；To solve in above-mentioned background technique
The problem of being previously mentioned.
To achieve the above object, the utility model provides the following technical solutions:
A kind of standardization dimensional structure of more case anaerobic organism contact deflector reactors, comprising: the first reaction chamber, second are instead
Answer room, third reaction chamber, the 4th reaction chamber, vertical baffle plate, inclined baffle, filler, overflow port, water outlet, reaction frame；
A kind of standardization dimensional structure of more case anaerobic organism contact deflector reactors, main body is by the first reaction chamber, second anti-
Answer room, third reaction chamber, the 4th reaction chamber this four reaction chambers composition: each reaction chamber is cement or steel build it is outdoor
Pond shape structure, this four reaction chambers of the first reaction chamber, the second reaction chamber, third reaction chamber, the 4th reaction chamber are arranged successively, and every two
Top between a reaction chamber is equipped with overflow port and is connected, and the direction of the non-third reaction chamber on the 4th reaction chamber is set
There is a water outlet.
As a further solution of the present invention: first reaction chamber, the second reaction chamber, third reaction chamber,
Four reaction chambers are equipped with reaction frame, filler and are suspended on reaction lower portion by the series connection of rope bunchiness, and reaction frame will be filled out
The institute of material composition filler string is supported and suspended；Filler is made of volcanic rock or sponge, and the diameter of filler is maintained at 80-
Between 150mm.
As a further solution of the present invention: being equipped with a vertical baffling below each reaction frame front end
Plate, the vertical baffle plate welding or bolt are fixed on the two sides of reaction chamber, fix clamped by the two sides by reaction chamber,
It is connected with an inclined baffle below vertical baffle plate, and inclined baffle welding simultaneously or bolt are fixed on the two of reaction chamber
Side, fixed clamped by the two sides by reaction chamber, length of the vertical baffle plate apart from reaction chamber front end is the baffling head of district
Degree.
As a further solution of the present invention: first reaction chamber, the second reaction chamber, third reaction chamber, the 4th
The length of reaction chamber is that D height is H, a length of L of the first reaction chamber1, the second reaction chamber a length of L2, third reaction chamber length
For L3, the 4th reaction chamber a length of L4, and L1~L4Length between 1/2D-1D, and L1> L2> L3> L4。
As a further solution of the present invention: the baffling section length is 1/5th of corresponding reaction chamber length,
Both l1~l4=1/5L1~1/5L4；Angle between the vertical baffle plate and inclined baffle of each baffling area lower end is α, and α
The angle of 1~α 4 is between 45 °~40 °, and 1 > α of α, 2 > α, 3 > α 4.
As a further solution of the present invention: each indoor vertical baffling board terminal of reaction is away from reactor bottom
Distance is h ', and h '=1/2l1。
As a further solution of the present invention: the height of the distance from bottom reaction chamber of each indoor reaction frame of reaction
Degree should be greater than 0.4H.
Sewage passes sequentially through overflow port and successively passes through the first reaction chamber, the second reaction chamber, third reaction chamber, the 4th when use
Reaction chamber, and reaction lower portion, H are rushed in the baffling area deflecting formed by vertical baffle plate, inclined baffle1~H4Point
Not Wei each first reaction chamber, the second reaction chamber, third reaction chamber, the 4th reaction chamber liquid level, the liquid of the reaction chamber of rear stage
Position is high should be high lower than the liquid level of the reaction chamber of rear stage, and liquid level difference control is between 10~20cm；React room temperature control
At 25~35 DEG C, hydraulic detention time is 36~72 hours；4th reaction chamber is equipped with reflux water pump, by the water in the 4th reaction chamber
The first reaction chamber is flowed back into microorganism；By multipoint water feeding, stablize the uniform water distribution problem of multiphase anaerobic baffled reactor, the
The Institute of Micro-biology that one reaction chamber, the second reaction chamber, third reaction chamber, the 4th reaction indoor sewage are adhered on filler decomposes,
Gas after decomposition, which directly passes through discharge, the sewage after being disposed above each reaction chamber, can pass through water outlet direct emission.
Compared with prior art, the utility model has the beneficial effects that
1. specifying each compartment parameter of multiphase anaerobic baffled reactor, (baffle plate angle, baffling section length, packing area are high
Degree, baffling board terminal is away from reactor bottom height) changing rule.
2. the ratio of each reaction chamber length, width and height of novel multi-phase anaerobic baffled reactor has been determined.
3. optimizing the distribution of concentration field, Flow and heat flux by multipoint water feeding.
4. solving the problems, such as anaerobic baffled reactor sludge loss by floating stuffing.
5. mitigating water inlet toxicity by internal reflux, improving biochemical efficiency.
Detailed description of the invention
Fig. 1 is that a kind of size of the standardization dimensional structure of more case anaerobic organism contact deflector reactors is distributed schematic diagram.
Fig. 2 is that a kind of size of the standardization dimensional structure of more case anaerobic organism contact deflector reactors is distributed schematic diagram.
In figure: the first reaction chamber of 1-, the second reaction chamber of 2-, 3- third reaction chamber, the 4th reaction chamber of 4-, the vertical baffling of 5-
Plate, 6- inclined baffle, 7- filler, 8- overflow port, 9- water outlet, 10- react frame.
Specific embodiment
The following will be combined with the drawings in the embodiments of the present invention, carries out the technical scheme in the embodiment of the utility model
Clearly and completely describe, it is clear that the described embodiments are only a part of the embodiments of the utility model, rather than whole
Embodiment；Based on the embodiments of the present invention, those of ordinary skill in the art are without making creative work
Every other embodiment obtained, fall within the protection scope of the utility model.
Please refer to Fig. 1~2, in the utility model embodiment, a kind of specification of more case anaerobic organism contact deflector reactors
Change dimensional structure, comprising: the first reaction chamber 1, the second reaction chamber 2, third reaction chamber 3, the 4th reaction chamber 4, vertical baffle plate 5,
Inclined baffle 6, filler 7, overflow port 8, water outlet 9, reaction frame 10；A kind of more case anaerobic organism contact deflectors are anti-
Answer the standardization dimensional structure of device, main body by the first reaction chamber 1, the second reaction chamber 2, third reaction chamber 3, the 4th reaction chamber 4 this
Four reaction chamber compositions: each reaction chamber is the outdoor pond shape structure that cement or steel are built, and the first reaction chamber 1, second is anti-
Room 2, third reaction chamber 3, the 4th reaction chamber 4 this four reaction chambers are answered to be arranged successively, the top between every two reaction chamber is all provided with
There is overflow port 8 to be connected, the direction of the non-third reaction chamber 3 on the 4th reaction chamber 4 is equipped with a water outlet 9.
First reaction chamber 1, the second reaction chamber 2, third reaction chamber 3, the 4th reaction chamber 4 are equipped with reaction frame
Frame 10, filler 7 are suspended on inside reaction frame 10 by the series connection of rope bunchiness, and filler 7 is formed the institute of filler string by reaction frame 10
It is supported and suspended；Filler 7 is made of volcanic rock or sponge, and the diameter of filler 7 is maintained between 80-150mm.
Be equipped with a vertical baffle plate 5 below each 10 front end of reaction frame, the vertical welding of baffle plate 5 or
Person's bolt is fixed on the two sides of reaction chamber, fixes clamped by the two sides by reaction chamber, is connected with one below vertical baffle plate 5
Inclined baffle 6, and the welding of inclined baffle 6 simultaneously or bolt are fixed on the two sides of reaction chamber, by the two sides of reaction chamber
Fixed clamped by side, length of the vertical baffle plate 5 apart from reaction chamber front end is baffling section length.
First reaction chamber 1, the second reaction chamber 2, third reaction chamber 3, the 4th reaction chamber 4 length be that D height is
H, a length of L of the first reaction chamber 11, the second reaction chamber 2 a length of L2, third reaction chamber 3 a length of L3, the 4th reaction chamber 4 length
For L4, and L1~L4Length between 1/2D-1D, and L1> L2> L3> L4。
The baffling section length is 1/5th of corresponding reaction chamber length, both l1~l4=1/5L1~1/5L4；Each folding
Angle between the vertical baffle plate 5 and inclined baffle 6 of the lower end Liu Qu is α, and the angle of 1~α of α 4 is between 45 °~40 °,
And 1 > α of α, 2 > α, 3 > α 4.
Indoor vertical distance of 5 terminal of baffle plate away from reactor bottom of each reaction is h ', and h '=1/2l1。
The height of the distance from bottom reaction chamber of each indoor reaction frame 10 of reaction should be greater than 0.4H.
When use sewage pass sequentially through overflow port 8 successively by the first reaction chamber 1, the second reaction chamber 2, third reaction chamber 3,
4th reaction chamber 4, and be rushed in reaction frame 10 in the baffling area deflecting formed by vertical baffle plate 5, inclined baffle 6
Portion, H1~H4The liquid level of respectively each first reaction chamber 1, the second reaction chamber 2, third reaction chamber 3, the 4th reaction chamber 4, it is latter
The liquid level height of the reaction chamber of grade should be high lower than the liquid level of the reaction chamber of rear stage, and liquid level difference control is between 10~20cm；Instead
Answer room temperature control at 25~35 DEG C, hydraulic detention time is 36~72 hours；4th reaction chamber 4 is equipped with reflux water pump, will
Water and microorganism in 4th reaction chamber 4 flow back into the first reaction chamber 1；By multipoint water feeding, stablize the anaerobic baffled reaction of multiphase
The uniform water distribution problem of device, the first reaction chamber 1, the second reaction chamber 2, third reaction chamber 3, the sewage in the 4th reaction chamber 4 are filled out
The Institute of Micro-biology adhered on material 7 decomposes, and the gas after decomposition directly passes through discharge, the dirt after being disposed above each reaction chamber
Water can pass through 9 direct emission of water outlet.
The working principle of the utility model is: using when sewage pass sequentially through overflow port and successively pass through the first reaction chamber,
Two reaction chambers, third reaction chamber, the 4th reaction chamber, and by vertical baffle plate, inclined baffle formed the deflecting of baffling area on
It is rushed to reaction lower portion, H1~H4Respectively each first reaction chamber, the second reaction chamber, third reaction chamber, the 4th reaction chamber
Liquid level, the liquid level height of the reaction chamber of rear stage should be high lower than the liquid level of the reaction chamber of rear stage, and liquid level difference control 10~
Between 20cm；Room temperature control is reacted at 25~35 DEG C, and hydraulic detention time is 36~72 hours；4th reaction chamber is equipped with
Flow back water pump, by the 4th reaction chamber water and microorganism flow back into the first reaction chamber；By multipoint water feeding, stablize multiphase anaerobism
The uniform water distribution problem of baffled reactor, the first reaction chamber, the second reaction chamber, third reaction chamber, the 4th indoor sewage of reaction
The Institute of Micro-biology adhered on filler decomposes, and the gas after decomposition directly passes through discharge above each reaction chamber, after being disposed
Sewage can pass through water outlet direct emission.
It is obvious to a person skilled in the art that the present invention is not limited to the details of the above exemplary embodiments, and
And without departing substantially from the spirit or essential attributes of the utility model, it can realize that this is practical new in other specific forms
Type；Therefore, in all respects, the present embodiments are to be considered as illustrative and not restrictive, this is practical new
The range of type is indicated by the appended claims rather than the foregoing description, it is intended that containing for the equivalent requirements of the claims will be fallen in
All changes in justice and range are embraced therein；It should not treat any reference in the claims as limiting
Related claim.
In addition, it should be understood that although this specification is described in terms of embodiments, but not each embodiment is only wrapped
Containing an independent technical solution, this description of the specification is merely for the sake of clarity, and those skilled in the art should
It considers the specification as a whole, the technical solutions in the various embodiments may also be suitably combined, forms those skilled in the art
The other embodiments being understood that.
Claims (7)
1. a kind of standardization dimensional structure of more case anaerobic organism contact deflector reactors, comprising: the first reaction chamber (1), second
Reaction chamber (2), the 4th reaction chamber (4), vertical baffle plate (5), inclined baffle (6), filler (7), overflows at third reaction chamber (3)
Head piece (8), water outlet (9), reaction frame (10)；It is characterized by: a kind of more case anaerobic organism contact deflector reactions
The standardization dimensional structure of device, main body is by the first reaction chamber (1), the second reaction chamber (2), third reaction chamber (3), the 4th reaction chamber
(4) this four reaction chamber compositions: the outdoor pond shape structure that each reaction chamber is built for cement or steel, the first reaction chamber (1),
Second reaction chamber (2), third reaction chamber (3), the 4th reaction chamber (4) this four reaction chambers are arranged successively, every two reaction chamber it
Between top be equipped with overflow port (8) and be connected, the direction of the non-third reaction chamber (3) on the 4th reaction chamber (4) is set
There is a water outlet (9).
2. a kind of standardization dimensional structure of more case anaerobic organism contact deflector reactors according to claim 1, special
Sign is: first reaction chamber (1), the second reaction chamber (2), third reaction chamber (3), the 4th reaction chamber (4) have installation
There are reaction frame (10), filler (7) to be suspended on reaction frame (10) inside by the series connection of rope bunchiness, reacts frame (10) for filler
(7) institute for forming filler string is supported and suspended；Filler (7) is made of volcanic rock or sponge, and the diameter of filler (7) is maintained at
Between 80-150mm.
3. a kind of standardization dimensional structure of more case anaerobic organism contact deflector reactors according to claim 1, special
Sign is: a vertical baffle plate (5), vertical baffle plate (5) weldering are equipped with below each reaction frame (10) front end
It connects or bolt is fixed on the two sides of reaction chamber, it is fixed clamped by the two sides by reaction chamber, connect below vertical baffle plate (5)
An inclined baffle (6) are connected to, and inclined baffle (6) welding simultaneously or bolt are fixed on the two sides of reaction chamber, it is anti-
It answers and is fixed clamped by the two sides of room, length of the vertical baffle plate (5) apart from reaction chamber front end is baffling section length.
4. a kind of standardization dimensional structure of more case anaerobic organism contact deflector reactors according to claim 1, special
Sign is: first reaction chamber (1), the second reaction chamber (2), third reaction chamber (3), the 4th reaction chamber (4) length be D
Height is H, a length of L of the first reaction chamber (1)1, the second reaction chamber (2) a length of L2, third reaction chamber (3) a length of L3, the 4th
A length of L of reaction chamber (4)4, and L1~L4Length between 1/2D-1D, and L1> L2> L3> L4。
5. a kind of standardization dimensional structure of more case anaerobic organism contact deflector reactors according to claim 3, special
Sign is: the baffling section length is 1/5th of corresponding reaction chamber length, both l1~l4=1/5L1~1/5L4；Each folding
Angle between the vertical baffle plate (5) and inclined baffle (6) of the lower end Liu Qu is α, and the angle of 1~α of α 4 is at 45 °~40 °
Between, and 1 > α of α, 2 > α, 3 > α 4.
6. a kind of standardization dimensional structure of more case anaerobic organism contact deflector reactors according to claim 3, special
Sign is: indoor vertical distance of baffle plate (5) terminal away from reactor bottom of each reaction is h ', and h '=1/2l1。
7. according to the standardization ruler of claim 2 and a kind of more case anaerobic organism contact deflector reactors as claimed in claim 4
Very little structure, it is characterised in that: the height of the distance from bottom reaction chamber of each indoor reaction frame (10) of reaction should be greater than
0.4H。
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN115246676A (en) * | 2022-07-01 | 2022-10-28 | 北京新城禹潞环保科技有限责任公司 | Gravity type small sewage treatment equipment |
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2018
- 2018-12-03 CN CN201822012207.7U patent/CN209481287U/en active Active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN115246676A (en) * | 2022-07-01 | 2022-10-28 | 北京新城禹潞环保科技有限责任公司 | Gravity type small sewage treatment equipment |
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