CN205874007U - Compound anaerobic reactor of baffling formula - Google Patents
Compound anaerobic reactor of baffling formula Download PDFInfo
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- CN205874007U CN205874007U CN201620814258.XU CN201620814258U CN205874007U CN 205874007 U CN205874007 U CN 205874007U CN 201620814258 U CN201620814258 U CN 201620814258U CN 205874007 U CN205874007 U CN 205874007U
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- anaerobic reactor
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Abstract
The utility model discloses a compound anaerobic reactor of baffling formula. Including box (15), in the box through a set of on baffle and a set of baffle down separate that the district (1) that becomes to intake just to sink, first order reaction district (2), one -level narrowband gas - water separation district (3), second order reaction distinguish (4), second grade narrowband gas - water separation distinguishes (5) and slurry separation zone (6), it is equipped with water inlet (7) to intake just to sink to distinguish, and slurry separation zone is equipped with delivery port (8), the box roof of going up baffle and box and going up between baffle and the last baffle is equipped with gas collection mouth (10), box bottom plate between baffle and box and lower baffle and the lower baffle is equipped with pai nikou (9) down, and painikou is equipped with blanking cover (11). The utility model discloses the difficult mud that produces of operation in -process blocks up and the deposit. Reactor operation in -process can not produce mud and run off, can improve the treatment effect.
Description
Technical field
This utility model relates to a kind of deflector type hybrid anaerobic reactor, belongs to technical field of sewage.
Background technology
Anaerobic reactor has been widely used in alcoholic waste water, dyeing waste water, municipal garbage waste water and biological system at present
The aspects such as hydrogen.But existing anaerobic reactor has the disadvantage that reactor bottom easily produces blocking and the deposition of mud.Instead
Answer and device running can produce sludge loss, cause treatment effect to reduce.
Summary of the invention
The purpose of this utility model is, it is provided that a kind of deflector type hybrid anaerobic reactor.To overcome prior art not enough.
The technical solution of the utility model:
A kind of deflector type hybrid anaerobic reactor, separates through one group of upper spacer and one group of lower clapboard including in casing, casing
Become water inlet Chu Chen district, first order reaction district, gas-water separation district, one-level arrowband, secondary response district, gas-water separation district, two grades of arrowbands and mud
Water Disengagement zone；Water inlet Chu Chen district is provided with water inlet, and mud-water separation district is provided with outlet；Upper spacer and casing and upper spacer are with upper
Roof box between dividing plate is provided with collection QI KOU；Box bottom between lower clapboard and casing and lower clapboard and lower clapboard is provided with
Mud discharging mouth, mud discharging mouth is provided with blanking cover.
In aforementioned deflector type hybrid anaerobic reactor, described water inlet is higher than outlet.
In aforementioned deflector type hybrid anaerobic reactor, described one group of upper spacer is connected with the top board of casing, one group of upper spacer
Including the upper spacer being arranged in order by water inlet to outlet, No. two upper spacers, No. three upper spacers, No. four upper spacers and five
Number upper spacer.
In aforementioned deflector type hybrid anaerobic reactor, described one group of lower clapboard is connected with the base plate of casing, including by intaking
A lower clapboard, No. two lower clapboards, No. three lower clapboards and No. four lower clapboards that mouth is arranged in order to outlet.
In aforementioned deflector type hybrid anaerobic reactor, a described upper spacer, No. three upper spacers, No. five upper spacers, No. two
Lower clapboard and No. four lower clapboards are flat board；No. two upper spacers and No. four upper spacers are U-shaped plate, are trapezium structure bottom U-shaped plate；
It is provided with one section of swash plate in the middle of a number lower clapboard and No. three lower clapboards；One section of swash plate in the middle of a number lower clapboard and No. three lower clapboards with
Bottom U-shaped plate, the swash plate correspondence on trapezium structure constitutes bell mouth.
In aforementioned deflector type hybrid anaerobic reactor, the tip height of a described lower clapboard be higher than No. two lower clapboards, two
The tip height of number lower clapboard is higher than No. four lower clapboards higher than No. three lower clapboards, the tip height of No. three lower clapboards.
In aforementioned deflector type hybrid anaerobic reactor, described one group of upper spacer and one group of lower clapboard interval are arranged；Under No. two
Spacing between dividing plate and No. two upper spacers and No. three upper spacers, and No. four lower clapboards and No. four upper spacers and No. five upper spacers
Between spacing be respectively less than the spacing between other dividing plate.
In aforementioned deflector type hybrid anaerobic reactor, in the casing of described outlet, it is provided with L-type overflow plate, L-type overflow plate
Tip height less than the tip height of No. four lower clapboards, and higher than water outlet height.
Compared with prior art, this utility model uses vertical polylith dividing plate that reactor is divided into two main reactions
District, two main reaction zones are similar to the anaerobic reactor without three phase separator of series connection.Stain disease is through pulling flow type warp step by step
Cross two main reaction zones, collection QI KOU is set at the top of each reactor, use up flow type flowing in narrow region, at a high speed
Precipitation and the blocking of mud is decreased, simultaneously by first order reaction district and gas-water separation district, one-level arrowband under promotion；And two grades
The microbial that reaction zone achieves anaerobic biological treatment with the design in gas-water separation district, two grades of arrowbands separates, and passes through waterpower
Learn and control and ecological regulation and control and nutriment chain close collaboration, organic by the macromolecule organic in waste water and difficult degradation
Thing decomposes step by step and converts.This utility model running is not likely to produce sludge blockage and deposition.In reactor running
Sludge loss will not be produced, treatment effect can be improved.
Accompanying drawing explanation
Fig. 1 is structural representation of the present utility model.
Being labeled as in figure: 1-water inlet Chu Chen district, 2-first order reaction district, gas-water separation district, 3-one-level arrowband, 4-bis-grades are instead
Answer district, gas-water separation district, bis-grades of arrowbands of 5-, 6-mud-water separation district, 7-water inlet, 8-outlet, 9-mud discharging mouth, 10-collection QI KOU,
11-blanking cover, 12-L type overflow plate, 13-swash plate, 14-bell mouth, 15-casing, number upper spacer of 21-, No. bis-upper spacers of 22-,
No. tri-upper spacers of 23-, No. tetra-upper spacers of 24-, No. five upper spacers of 25-, number lower clapboard of 31-, No. bis-lower clapboards of 32-, 33-tri-
Lower clapboard, No. tetra-lower clapboards of 34-.
Detailed description of the invention
The utility model is described in further detail with embodiment below in conjunction with the accompanying drawings, but not as new to this practicality
Any restriction of type.
A kind of deflector type hybrid anaerobic reactor, as it is shown in figure 1, include casing 15, in casing 15 through one group of upper spacer and
One group of lower clapboard is separated into Jin Shuichuchen district 1, first order reaction district 2, gas-water separation district, one-level arrowband 3,4, two grades of secondary response district
Gas-water separation district, arrowband 5 and mud-water separation district 6；Water inlet Chu Chen district 1 is provided with water inlet 7, and mud-water separation district 6 is provided with outlet 8；On
Casing 15 top board between dividing plate and casing 15 and upper spacer and upper spacer is provided with collection QI KOU 10；Lower clapboard and casing 15 and
Casing 15 base plate between lower clapboard and lower clapboard is provided with mud discharging mouth 9, and mud discharging mouth 9 is provided with blanking cover 11.Water inlet 7 is higher than outlet
8.One group of upper spacer is connected with the top board of casing 15, and one group of upper spacer includes No. be arranged in order by water inlet 7 to outlet 8
21, No. two upper spacers of upper spacer, 23, No. four upper spacers 24 of 22, No. three upper spacers and No. five upper spacers 25.One group of lower clapboard and case
The base plate of body 15 connects, including 31, No. two lower clapboards of the lower clapboard being arranged in order by water inlet 7 to outlet 8 32, three
Lower clapboard 33 and No. four lower clapboards 34.21, No. three upper spacers of a number upper spacer, 25, No. two lower clapboard 32 and of 23, No. five upper spacers
No. four lower clapboards 34 are flat board；No. two upper spacers 22 and No. four upper spacers 24 are U-shaped plate, are trapezium structure bottom U-shaped plate；One
It is provided with one section of swash plate 13 in the middle of number lower clapboard 31 and No. three lower clapboards 33；In the middle of a number lower clapboard 31 and No. three lower clapboards 33 one
Composition corresponding with the swash plate 13 on trapezium structure bottom the U-shaped plate bell mouth 14 of section swash plate 13.The tip height of a number lower clapboard 31
Higher than No. two lower clapboards 32, the tip height of No. two lower clapboards 32 is higher than No. three lower clapboards 33, and the top of No. three lower clapboards 33 is high
Degree is higher than No. four lower clapboards 34.One group of upper spacer and one group of lower clapboard interval are arranged；No. two lower clapboards 32 and No. two upper spacers 22
And between the spacing between No. three upper spacers 23, and No. four lower clapboards 34 and No. four upper spacers 24 and No. five upper spacers 25
Away from the spacing being respectively less than between other dividing plate.Being provided with L-type overflow plate 12 in the casing of outlet 8, the top of L-type overflow plate 12 is high
Degree is less than the tip height of No. four lower clapboards 34, and is higher than outlet 8 height.
Embodiment
As it is shown in figure 1, this example is the integrated apparatus improved, through test repeatedly and calculating, devise two mainly
Reaction zone, while reducing reactor size, improve the disposal ability of system.First order reaction district 2 He in the middle part of reactor
Secondary response district 4 imitates three-phase separator device, is used in the separation of liquid by gas collecting apparatus, it is therefore prevented that the loss of mud, increases
The granulating of mud is formed.Double slanted design bottom first order reaction district 2 and secondary response district 4, effectively prevent mud
Blocking and deposition.First order reaction district, gas-water separation district, one-level arrowband, secondary response district and the different chi in gas-water separation district, two grades of arrowbands
The design of very little size so that mud flow at high speed in narrow compartment advances, and in wide compartment, low speed deposition and granulating, improve whole
The impact resistance of individual device.This example is the design of many compartments, it is achieved mud and the separation of sewage.Water outlet uses spilling to set
Meter, effectively raises the water quality of water outlet.
Work process of the present utility model and principle
Sewage is entered the casing 15 of reactor by water inlet 7, and the sewage after process is discharged by outlet 8, in whole reaction
Device is provided with two main reaction zones, first order reaction district 2 and secondary response district 4, owing to sewage plug-flow in the reactor is carried out,
Causing the microbial in the two reaction zone entirely different, the effect of process is the most different, the Main Function in first order reaction district 2
Being to be the sewage of low concentration by the biochemical wastewater treatment of high concentration, the Main Function in secondary response district 4 is by the sewage of low concentration
It is degraded to discharge standard.The arrowband in gas-water separation district, one-level arrowband 3 and gas-water separation district, two grades of arrowbands 5 is mainly designed to for dirt
The separation of air water in water, the Main Function in mud-water separation district 6 is to realize mud-water separation, the overflow discharge design of supernatant, effectively
The sewage treatment capacity that improve device.
Claims (8)
1. a deflector type hybrid anaerobic reactor, it is characterised in that: include casing (15), through one group of upper spacer in casing (15)
It is separated into Jin Shuichuchen district (1), first order reaction district (2), gas-water separation district, one-level arrowband (3), secondary response with one group of lower clapboard
District (4), gas-water separation district, two grades of arrowbands (5) and mud-water separation district (6)；Water inlet Chu Chen district (1) is provided with water inlet (7), and muddy water divides
It is provided with outlet (8) from district (6)；Casing (15) top board between upper spacer and casing (15) and upper spacer and upper spacer is provided with
Collection QI KOU (10)；Casing (15) base plate between lower clapboard and casing (15) and lower clapboard and lower clapboard is provided with mud discharging mouth (9),
Mud discharging mouth (9) is provided with blanking cover (11).
Deflector type hybrid anaerobic reactor the most according to claim 1, it is characterised in that: described water inlet (7) is higher than water outlet
Mouth (8).
Deflector type hybrid anaerobic reactor the most according to claim 2, it is characterised in that: described one group of upper spacer and casing
(15) top board connects, a upper spacer (21) that one group of upper spacer includes being arranged in order by water inlet (7) to outlet (8),
No. two upper spacers (22), No. three upper spacers (23), No. four upper spacers (24) and No. five upper spacers (25).
Deflector type hybrid anaerobic reactor the most according to claim 3, it is characterised in that: described one group of lower clapboard and casing
(15) base plate connects, including the lower clapboard (31) being arranged in order by water inlet (7) to outlet (8), No. two lower clapboards
(32), No. three lower clapboards (33) and No. four lower clapboards (34).
Deflector type hybrid anaerobic reactor the most according to claim 4, it is characterised in that: a described upper spacer (21), three
Number upper spacer (23), No. five upper spacers (25), No. two lower clapboards (32) and No. four lower clapboards (34) are flat board；No. two upper spacers
(22) and No. four upper spacers (24) are U-shaped plate, are trapezium structure bottom U-shaped plate；A number lower clapboard (31) and No. three lower clapboards
(33) it is provided with one section of swash plate (13) in the middle of；One section of swash plate (13) in the middle of a number lower clapboard (31) and No. three lower clapboards (33) and U
Bottom template, the swash plate on trapezium structure (13) is corresponding constitutes bell mouth (14).
Deflector type hybrid anaerobic reactor the most according to claim 5, it is characterised in that: the top of a described lower clapboard (31)
End height is higher than No. two lower clapboards (32), and the tip height of No. two lower clapboards (32) is higher than No. three lower clapboards (33), under No. three every
The tip height of plate (33) is higher than No. four lower clapboards (34).
Deflector type hybrid anaerobic reactor the most according to claim 6, it is characterised in that: under described one group of upper spacer and one group
Baffle interval is arranged；Spacing between No. two lower clapboards (32) and No. two upper spacers (22) and No. three upper spacers (23), Yi Jisi
Between spacing number between lower clapboard (34) and No. four upper spacers (24) and No. five upper spacers (25) is respectively less than between other dividing plate
Away from.
Deflector type hybrid anaerobic reactor the most according to claim 7, it is characterised in that: in the casing of described outlet (8)
Being provided with L-type overflow plate (12), the tip height of L-type overflow plate (12) is less than the tip height of No. four lower clapboards (34), and is higher than
Outlet (8) is highly.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620814258.XU CN205874007U (en) | 2016-07-31 | 2016-07-31 | Compound anaerobic reactor of baffling formula |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620814258.XU CN205874007U (en) | 2016-07-31 | 2016-07-31 | Compound anaerobic reactor of baffling formula |
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| Publication Number | Publication Date |
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| CN205874007U true CN205874007U (en) | 2017-01-11 |
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| Application Number | Title | Priority Date | Filing Date |
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| CN201620814258.XU Active CN205874007U (en) | 2016-07-31 | 2016-07-31 | Compound anaerobic reactor of baffling formula |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106746387A (en) * | 2017-03-31 | 2017-05-31 | 河南工程学院 | A kind of decentralized sewage treatment method |
| CN110894125A (en) * | 2019-09-25 | 2020-03-20 | 镇江新纳环保材料有限公司 | Sewage treatment process for recycling N-methyl pyrrolidone |
-
2016
- 2016-07-31 CN CN201620814258.XU patent/CN205874007U/en active Active
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106746387A (en) * | 2017-03-31 | 2017-05-31 | 河南工程学院 | A kind of decentralized sewage treatment method |
| CN106746387B (en) * | 2017-03-31 | 2020-05-12 | 河南工程学院 | Distributed sewage treatment method |
| CN110894125A (en) * | 2019-09-25 | 2020-03-20 | 镇江新纳环保材料有限公司 | Sewage treatment process for recycling N-methyl pyrrolidone |
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