CN206538255U - A kind of UASB anaerobic reactors - Google Patents
A kind of UASB anaerobic reactors Download PDFInfo
- Publication number
- CN206538255U CN206538255U CN201720274171.2U CN201720274171U CN206538255U CN 206538255 U CN206538255 U CN 206538255U CN 201720274171 U CN201720274171 U CN 201720274171U CN 206538255 U CN206538255 U CN 206538255U
- Authority
- CN
- China
- Prior art keywords
- pole
- baffle plate
- separator
- water
- phase
- 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 - Fee Related
Links
- 238000009280 upflow anaerobic sludge blanket technology Methods 0.000 title claims abstract description 20
- 239000007788 liquid Substances 0.000 claims abstract description 33
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 29
- 239000010865 sewage Substances 0.000 claims abstract description 19
- 238000000926 separation method Methods 0.000 claims abstract description 7
- 238000003756 stirring Methods 0.000 claims description 22
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 claims description 10
- 239000011148 porous material Substances 0.000 claims description 7
- 238000009826 distribution Methods 0.000 claims description 2
- 230000001788 irregular Effects 0.000 claims description 2
- JEGUKCSWCFPDGT-UHFFFAOYSA-N h2o hydrate Chemical compound O.O JEGUKCSWCFPDGT-UHFFFAOYSA-N 0.000 claims 1
- 239000010802 sludge Substances 0.000 abstract description 17
- 239000007787 solid Substances 0.000 abstract description 6
- 239000000463 material Substances 0.000 abstract description 5
- 239000000945 filler Substances 0.000 abstract description 3
- 238000010907 mechanical stirring Methods 0.000 abstract description 3
- 238000010992 reflux Methods 0.000 abstract description 3
- 238000004062 sedimentation Methods 0.000 abstract description 3
- 230000000630 rising effect Effects 0.000 abstract 1
- 239000007789 gas Substances 0.000 description 11
- 239000008187 granular material Substances 0.000 description 7
- 230000000694 effects Effects 0.000 description 5
- 239000002245 particle Substances 0.000 description 3
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 2
- 230000015572 biosynthetic process Effects 0.000 description 2
- 238000000746 purification Methods 0.000 description 2
- 239000002351 wastewater Substances 0.000 description 2
- 208000033999 Device damage Diseases 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 229910002092 carbon dioxide Inorganic materials 0.000 description 1
- 239000001569 carbon dioxide Substances 0.000 description 1
- 238000004140 cleaning Methods 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 238000013461 design Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 230000003670 easy-to-clean Effects 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 230000002349 favourable effect Effects 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 239000005416 organic matter Substances 0.000 description 1
- 239000002244 precipitate Substances 0.000 description 1
- 230000011514 reflex Effects 0.000 description 1
- 230000000717 retained effect Effects 0.000 description 1
- 239000013049 sediment Substances 0.000 description 1
- 230000035939 shock Effects 0.000 description 1
- 230000006641 stabilisation Effects 0.000 description 1
- 238000011105 stabilization Methods 0.000 description 1
- 238000012546 transfer Methods 0.000 description 1
Classifications
-
- 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
Landscapes
- Purification Treatments By Anaerobic Or Anaerobic And Aerobic Bacteria Or Animals (AREA)
Abstract
The utility model is related to a kind of UASB anaerobic reactors, including tank body and cyclone gas-liquid separator；The tank interior is disposed with two pole three phase separators, a pole three phase separator and water-locator from top to bottom；The water-locator is laid in tank body bottom inner portion, and the water-locator lower end is connected with sewage water inlet pipe, and the sewage water inlet pipe is overhanging through tank body port；By setting water-locator that sewage is uniformly distributed being dealt on the cross section of reactor and uniformly rising；By setting a pole three phase separator and two pole three phase separators effectively to be separated gas, liquid and the class material of solid three；By setting cyclone gas-liquid separator effectively to be discharged after biogas and water separation；The utility model equipment is simple, and operation is convenient, does not need to set sedimentation basin and sludge refluxing apparatus, it is not necessary to fill filler, is also not required in reaction zone set mechanical stirring device, cost is relatively low, is easy to management, and in the absence of blockage problem.
Description
Technical field
The utility model belongs to technical field of sewage treatment equipment, and in particular to a kind of UASB anaerobic reactors.
Background technology
UASB reactors waste water is uniformly introduced the bottom of reactor as far as possible, and sewage is upwardly through including granule sludge
Or the Sludge Bed of floc sludge.The process contacted in waste water and mud granule occurs for anaerobic reaction.Produced under anaerobic state
Biogas (mainly methane and carbon dioxide) causes the circulation of inside, and this is favourable for the formation and maintenance of granule sludge.
Some gases of sludge blanket formation are attached on mud granule, and attachment and the gas without attachment rise to reactor head.On
The sludge for being raised to surface hits the bottom of phase reactor gas launcher, causes the sludge flco of bubbles attached to deaerate.Bubble
Mud granule will be deposited to the surface of Sludge Bed after release, and attachment and the gas without attachment are collected into the three of reactor head
The collection chamber of phase separator.The acting as of the baffle plate being placed under collection chamber unit interstices and prevents biogas bubble at gas launcher
Into settling zone, otherwise the wadding for causing settling zone is moved, particle can be hindered to precipitate.Comprising some remaining solids and mud granule
Liquid enters settling zone by separator gap.
Because the area of passage of the skew wall settling zone of separator increases when close to the water surface, therefore upflow velocity is in close row
Put a reduction.Because flow velocity reduction sludge flco can flocculate and precipitate in settling zone.Accumulate the sludge on three phase separator
The frictional force that flco will be maintained on skew wall more than it to a certain extent, it will slide back to reaction zone, and this partial sludge again will be with
Entering organic matter of water reacts.
The application number that existing Chinese reactor such as Chinese patent is announced：02282323.9, utility model title：Interior circulation
Anaerobism is expanded bed/fluidized-bed reactor, the reactor technical characteristics are to build gas-liquid separation zone with second reaction zone jointly, top
Portion's part is as being gas-liquid separation zone, and second reaction zone does not set three phase separator, using the bigger annular Jiang Liu areas of area.Should
Patent reactor still can form interior circulation, but structure is greatly simplified.But the patent is disadvantageous in that：Carrier current consumes energy
Consumption is big, and the design requirement of system is high, and purification efficiency is low, and internal dirt cleaning is inconvenient, is easily caused device damage, reducing makes
Use the life-span.
For problem above, therefore, it is necessary to make improvements.
Utility model content
The utility model be in order to overcome above-mentioned defect of the prior art there is provided one kind it is simple in construction, it is easy to use, easily
In operation, waterpower adjustment is convenient, and mass transfer effect is good, and sludge can be effectively retained in the UASB anaerobic reactors in reactor.
In order to reach object above, the technical scheme that the utility model is used is：A kind of UASB anaerobic reactors, including
Tank body and cyclone gas-liquid separator；The tank interior is disposed with two pole three phase separators, a pole three-phase separate from top to bottom
From device and water-locator；The water-locator is laid in tank body bottom inner portion, and the water-locator lower end is connected with sewage water inlet pipe, described
Sewage water inlet pipe is overhanging through tank body port；The cyclone gas-liquid separator upper end is provided with collecting methane pipe, the cyclone gas
Liquid/gas separator side is provided with outlet pipe；The tank interior center leads to the decline of water-locator provided with spin current gas-liquid separator
Pipe, pole three phase separator is provided with the tedge communicated with two pole three phase separators, two pole three phase separator
Provided with the discharge for leading to cyclone gas-liquid separator.
As a kind of preferred scheme of the present utility model, the cyclone gas-liquid separator includes shell separator, agitating shaft,
Stirring motor and stirring vane；The top half of the shell separator is taper, and lower portion is cylindrical shape；Shell separator
Bottom be connected with connecting plate；Down-comer is connected with discharge through connecting plate with shell separator, and the agitating shaft is rotated
The axial location of shell separator top half is installed on, the upper end of the agitating shaft is connected with stirring motor, the agitating shaft
Lower end is connected with stirring vane, and stirring vane is located in the lower portion of shell separator, stirring vane and down-comer and gas collection
Certain distance is left between pipe.
As a kind of preferred scheme of the present utility model, the water-locator includes being in coniform housing, described housing
In accommodating cavity is provided with hollow form and its, accommodating cavity is connected with sewage water inlet pipe, and described case top is connected with down-comer；Shell
Multiple water distributing pores are offered on body, water distributing pore is equidistantly laid on housing.
As a kind of preferred scheme of the present utility model, pole three phase separator and two pole three phase separators are removable
It is connected in tank body, and a pole three phase separator is identical with two pole three phase separator structures.
As a kind of preferred scheme of the present utility model, pole three phase separator includes downward opening multiple V-arrangements
Baffle plate and the gas-collecting pipe located at two ends at the top of V-arrangement baffle plate；Connecting tube is provided between V-arrangement baffle plate and gas-collecting pipe；Connection
Pipe is positioned at the top of V-arrangement baffle plate；Connecting tube is connected with gas-collecting pipe；The V-arrangement baffle plate is by left-leaning baffle plate and Right deviation baffle plate
Combined according to the angle of setting；Multiple V-arrangement baffle plates are divided into group and the following group, and every group of V-arrangement baffle plate parallel interval is set, two groups
V-arrangement baffle plate is staggered.
As a kind of preferred scheme of the present utility model, pole three phase separator includes seven V-arrangement baffle plates, upper group of bag
Three V-arrangement baffle plates are included, the following group includes four V-arrangement baffle plates, and upper group of V-arrangement baffle plate is between two V-arrangement baffle plates of the following group.
As a kind of preferred scheme of the present utility model, parallel gear is connected between the left-leaning baffle plate and Right deviation baffle plate
Plate；The left-leaning baffle plate, Right deviation baffle plate are fixedly connected with parallel baffle, are integrally formed；The width of parallel baffle and connecting tube
External diameter is consistent.
As a kind of preferred scheme of the present utility model, the cross section of the discharge is ellipse, polygon or by
The irregular shape of line segment and camber line composition.
As a kind of preferred scheme of the present utility model, described adjacent two levels of V-arrangement baffle plate being staggered are thrown
Shadow overlapped 10%~30%.
As a kind of preferred scheme of the present utility model, the angle of the V-arrangement baffle plate is 70~120 °.
The beneficial effects of the utility model are：By setting water-locator that sewage is uniformly distributed to be dealt into the cross-section of reactor
Rise on face and uniformly；By setting a pole three phase separator and two pole three phase separators effectively by gas, liquid and solid three
Class material is separated；By setting cyclone gas-liquid separator effectively to be discharged after biogas and water separation；The utility model is set
Standby simple, operation is convenient, does not need to set sedimentation basin and sludge refluxing apparatus, it is not necessary to fill filler, is also not required to set in reaction zone
Mechanical stirring device, cost is relatively low, is easy to management, and in the absence of blockage problem.
Brief description of the drawings
Fig. 1 is example structure sectional view of the present utility model；
Fig. 2 is example structure schematic diagram of the present utility model；
Fig. 3 is the pole three phase separator structural representation of embodiment one of the present utility model；
Reference in figure：Tank body 1, cyclone gas-liquid separator 2, shell separator 2-1, agitating shaft 2-2, stirring motor 2-
3, stirring vane 2-4, connecting plate 2-5, two pole three phase separators 3, a pole three phase separator 4, V-arrangement baffle plate 4-1, left-leaning baffle plate 4-
1-1, Right deviation baffle plate 4-1-2, parallel baffle 4-1-3, gas-collecting pipe 4-2, connecting tube 4-3, water-locator 5, housing 5-1 are housed
Chamber 5-2, water distributing pore 5-3, sewage water inlet pipe 6, collecting methane pipe 7, outlet pipe 8, down-comer 9, tedge 10, discharge 11, even
Joint chair 12.
Embodiment
The utility model embodiment is elaborated below in conjunction with the accompanying drawings.
Embodiment one：As Figure 1-3, a kind of UASB anaerobic reactors, including tank body 1 and cyclone gas-liquid separator 2；Tank
The bottom of body 1, which is socketed with around connecting seat 12, connecting seat 12, is evenly equipped with bolt hole, and connecting seat 12 and ground can pass through bolt arrangement
It is fixedly connected；Significant shock is produced when preventing the UASB anaerobic reactors from working；Two are disposed with from top to bottom inside tank body 1
Pole three phase separator 3, a pole three phase separator 4 and water-locator 5；Water-locator 5 is laid in the bottom inner portion of tank body 1, the lower end of water-locator 5
Sewage water inlet pipe 6 is connected with, sewage water inlet pipe 6 is overhanging through the port of tank body 1；The upper end of cyclone gas-liquid separator 2 is provided with biogas
Collecting pipe 7, the side of cyclone gas-liquid separator 2 is provided with outlet pipe 8；The inside center of tank body 1 is logical provided with spin current gas-liquid separator 2
Toward the down-comer 9 of water-locator 5, a pole three phase separator 4 is provided with the tedge 10 communicated with two pole three phase separators 3, two poles
Three phase separator 3 is provided with the discharge 11 for leading to cyclone gas-liquid separator 2；The shape of cross section of discharge 11 can be according to reality
Border needs to be designed, and the cross section than discharge as shown in Figure 1 is circle；Sewage is equably divided by setting water-locator 5
It is dispensed on the cross section of reactor and uniformly rises；By setting a pole three phase separator 4 and two pole three phase separators 3 effective
Gas, liquid and the class material of solid three are separated；By setting cyclone gas-liquid separator 2 effectively to separate biogas and water
After discharge；The utility model equipment is simple, and operation is convenient, does not need to set sedimentation basin and sludge refluxing apparatus, it is not necessary to fill filler,
Also it is not required in reaction zone set mechanical stirring device, cost is relatively low, is easy to management, and in the absence of blockage problem.
Cyclone gas-liquid separator 2 includes shell separator 2-1, agitating shaft 2-2, stirring motor 2-3 and stirring vane 2-4；
Shell separator 2-1 top half is taper, and lower portion is cylindrical shape；Shell separator 2-1 bottom is connected with connection
Plate 2-5；Down-comer 9 is connected with discharge 11 through connecting plate 2-5 with shell separator 2-1, agitating shaft 2-2 be rotatablely installed in
The axial location of shell separator 2-1 top halfs, agitating shaft 2-2 upper end is connected with stirring motor 2-3, agitating shaft 2-2
End is connected with stirring vane 2-4, and stirring vane 2-4 is located in shell separator 2-1 lower portion, and stirring vane 2-4 is with
Certain distance is left between drop pipe 9 and discharge 11；By setting cyclone gas-liquid separator effectively by after biogas and water separation
Discharge, improves purification efficiency.
Water-locator 5 includes being in coniform housing 5-1, and housing 5-1 is housed in accommodating cavity 5-2 is provided with hollow form and its
Chamber 5-2 is connected with sewage water inlet pipe 6, and down-comer 9 is connected with the top of housing 5-1；Multiple water distributing pore 5-3 are offered on housing 5-1,
Water distributing pore 5-3 is equidistantly laid on housing 5-1；Sewage and the material blended, resistance reflex in the accommodating cavity 5-2 of water-locator 5
Turbulent flow is formed afterwards, so as to realize the purpose of material water mixing, is reached the effect of water distribution uniformity, is effectively increased Biochemical Treatment.
One pole three phase separator 4 and two pole three phase separators 3 are removably coupled in tank body 1, are easy to clean and are installed
It is convenient, improve the service efficiency of a pole three phase separator 4 and two pole three phase separators 3, a pole three phase separator 4 and two poles three
The structure of phase separator 3 is identical.
One pole three phase separator 4 includes downward opening multiple V-arrangement baffle plate 4-1 and located at two ends at the top of V-arrangement baffle plate 4-1
Gas-collecting pipe 4-2；Connecting tube 4-3 is provided between V-arrangement baffle plate 4-1 and gas-collecting pipe 4-2；Connecting tube 4-3 is located at V-arrangement baffle plate
4-1 top；Connecting tube 4-3 is connected with gas-collecting pipe 4-2；The V-arrangement baffle plate 4-1 is by left-leaning baffle plate 4-1-1 and Right deviation
Baffle plate 4-1-2 is combined according to the angle of setting；Multiple V-arrangement baffle plate 4-1 points are upper group and the following group, and every group of V-arrangement baffle plate 4-1 is put down
Between-line spacing is set, and two groups of V-arrangement baffle plate 4-1 are staggered；One pole three phase separator 4 includes seven V-arrangement baffle plate 4-1, and upper group includes
Three V-arrangement baffle plate 4-1, the following group includes four V-arrangement baffle plates 4-1, upper group of V-arrangement baffle plate 4-1 and is located at two V-arrangement baffle plate 4- of the following group
Between 1；One pole three phase separator 4 can neatly set up V-arrangement baffle plate 4-1 quantity, and multiple resistance can be played by setting up baffle number
Every the effect of solid particle in sewage, the water for flowing to separator bottom is set to reduce solid particle as far as possible.Therefore, in increase baffle plate
While quantity, the height of tank body 1 of UASB anaerobic reactors also can accordingly increase, it is necessary to when reequiping, need to only hang in and add by baffle plate
Installed in high tank body 1.
Parallel baffle 4-1-3 is connected between left-leaning baffle plate 4-1-1 and Right deviation baffle plate 4-1-2；The left-leaning baffle plate 4-1-
1st, Right deviation baffle plate 4-1-2 is fixedly connected with parallel baffle 4-1-3, is integrally formed；Parallel baffle 4-1-3 width and connecting tube 4-
3 external diameter is consistent；Parallel baffle 4-1-3 is set, mud granule can be prevented to be raised current and take away, is conducive to the heavy of sludge
Form sediment.
The floor projection overlapped 10%~30% for the V-arrangement baffle plate 4-1 that adjacent two are staggered；Gas-liquid to be reached
Purpose is separated, two groups of V-arrangement baffle plate 4-1 inclined-plane must be overlapping up and down, and overlapping floor projection is bigger, and the separating effect of gas is got over
It is good, go the diameter of bubble removing smaller, the influence to settling zone solid-liquid separation effect is smaller；V-arrangement baffle plate 4-1 angle is 70~
120 °, more preferably 90 DEG C.Such angle sets and may be such that the sludge being deposited on V-arrangement baffle plate 4-1 slopes smoothly glides, together
When can keep the stabilization of current.
The foregoing description of the disclosed embodiments, enables professional and technical personnel in the field to realize or new using this practicality
Type.A variety of modifications to these embodiments will be apparent for those skilled in the art, determine herein
The General Principle of justice can in other embodiments be realized in the case where not departing from spirit or scope of the present utility model；Cause
This, the utility model is not intended to be limited to the embodiments shown herein, and is to fit to and principles disclosed herein
The most wide scope consistent with features of novelty.
Although more having used reference in figure herein：Tank body 1, cyclone gas-liquid separator 2, shell separator 2-1,
Agitating shaft 2-2, stirring motor 2-3, stirring vane 2-4, connecting plate 2-5, two pole three phase separators 3, a pole three phase separator 4, V
Shape baffle plate 4-1, left-leaning baffle plate 4-1-1, Right deviation baffle plate 4-1-2, parallel baffle 4-1-3, gas-collecting pipe 4-2, connecting tube 4-3,
Water-locator 5, housing 5-1, accommodating cavity 5-2, water distributing pore 5-3, sewage water inlet pipe 6, collecting methane pipe 7, outlet pipe 8, down-comer 9,
Tedge 10, discharge 11, the grade term of connecting seat 12, but it is not precluded from the possibility using other terms.Use these terms
Just for the sake of more easily describing and explaining essence of the present utility model；It is construed as any additional limitation all
Disagreed with the utility model spirit.
Claims (10)
1. a kind of UASB anaerobic reactors, it is characterised in that：Including tank body (1) and cyclone gas-liquid separator (2)；The tank body
(1) it is internal to be disposed with two pole three phase separators (3), a pole three phase separator (4) and water-locator (5) from top to bottom；It is described
Water-locator (5) is laid in tank body (1) bottom inner portion, and water-locator (5) lower end is connected with sewage water inlet pipe (6), the sewage
Water inlet pipe (6) is overhanging through tank body (1) port；Cyclone gas-liquid separator (2) upper end is provided with collecting methane pipe (7), institute
State cyclone gas-liquid separator (2) side and be provided with outlet pipe (8)；Tank body (1) inside center is provided with spin current gas-liquid separation
Device (2) leads to the down-comer (9) of water-locator (5), and pole three phase separator (4) is provided with and two pole three phase separators (3)
The tedge (10) communicated, two pole three phase separator (3) is provided with the discharge for leading to cyclone gas-liquid separator (2)
(11)。
2. a kind of UASB anaerobic reactors according to claim 1, it is characterised in that：The cyclone gas-liquid separator (2)
Including shell separator (2-1), agitating shaft (2-2), stirring motor (2-3) and stirring vane (2-4)；The shell separator
The top half of (2-1) is taper, and lower portion is cylindrical shape；The bottom of shell separator (2-1) is connected with connecting plate (2-
5)；Down-comer (9) is connected with discharge (11) through connecting plate (2-5) with shell separator (2-1), the agitating shaft (2-
2) it is rotatablely installed in the axial location of shell separator (2-1) top half, the upper end of the agitating shaft (2-2) is connected with stirring
Motor (2-3), agitating shaft (2-2) lower end is connected with stirring vane (2-4), and stirring vane (2-4) is located at shell separator
In the lower portion of (2-1), certain distance is left between stirring vane (2-4) and down-comer (9) and discharge (11).
3. a kind of UASB anaerobic reactors according to claim 1, it is characterised in that：The water-locator (5) is included in circle
The housing (5-1) of taper, described housing (5-1) is in hollow form and it is interior provided with accommodating cavity (5-2), accommodating cavity (5-2) and dirt
Water water inlet pipe (6) is connected, and down-comer (9) is connected with the top of described housing (5-1)；Multiple water distributions are offered on housing (5-1)
Hole (5-3), water distributing pore (5-3) is equidistantly laid on housing (5-1).
4. a kind of UASB anaerobic reactors according to claim 1, it is characterised in that：One pole three phase separator (4)
It is removably coupled to two pole three phase separators (3) in tank body (1), and a pole three phase separator (4) and two pole three phase separators
(3) structure is identical.
5. a kind of UASB anaerobic reactors according to claim 4, it is characterised in that：One pole three phase separator (4)
Gas-collecting pipe (4-2) including downward opening multiple V-arrangement baffle plates (4-1) and located at two ends at the top of V-arrangement baffle plate (4-1)；V-arrangement
Connecting tube (4-3) is provided between baffle plate (4-1) and gas-collecting pipe (4-2)；Connecting tube (4-3) is located at the top of V-arrangement baffle plate (4-1)
Portion；Connecting tube (4-3) is connected with gas-collecting pipe (4-2)；The V-arrangement baffle plate (4-1) is by left-leaning baffle plate (4-1-1) and Right deviation
Baffle plate (4-1-2) is combined according to the angle of setting；Multiple V-arrangement baffle plates (4-1) are divided into group and the following group, every group of V-arrangement baffle plate
(4-1) parallel interval is set, and two groups of V-arrangement baffle plates (4-1) are staggered.
6. a kind of UASB anaerobic reactors according to claim 5, it is characterised in that：One pole three phase separator (4)
Including seven V-arrangement baffle plates (4-1), upper group includes three V-arrangement baffle plates (4-1), and the following group includes four V-arrangement baffle plates (4-1), upper group
V-arrangement baffle plate (4-1) is between two V-arrangement baffle plates (4-1) of the following group.
7. a kind of UASB anaerobic reactors according to claim 5, it is characterised in that：The left-leaning baffle plate (4-1-1) and
Parallel baffle (4-1-3) is connected between Right deviation baffle plate (4-1-2)；The left-leaning baffle plate (4-1-1), Right deviation baffle plate (4-1-2)
It is fixedly connected, is integrally formed with parallel baffle (4-1-3)；The width of parallel baffle (4-1-3) and the external diameter phase of connecting tube (4-3)
Unanimously.
8. a kind of UASB anaerobic reactors according to claim 1 or 2, it is characterised in that：The horizontal stroke of the discharge (11)
Section is ellipse, polygon or the irregular shape being made up of line segment and camber line.
9. a kind of UASB anaerobic reactors according to claim 6, it is characterised in that：Described adjacent two are staggered
V-arrangement baffle plate (4-1) floor projection overlapped 10%~30%.
10. a kind of UASB anaerobic reactors according to claim 9, it is characterised in that：The folder of the V-arrangement baffle plate (4-1)
Angle is 70~120 °.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720274171.2U CN206538255U (en) | 2017-03-20 | 2017-03-20 | A kind of UASB anaerobic reactors |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720274171.2U CN206538255U (en) | 2017-03-20 | 2017-03-20 | A kind of UASB anaerobic reactors |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206538255U true CN206538255U (en) | 2017-10-03 |
Family
ID=59943000
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201720274171.2U Expired - Fee Related CN206538255U (en) | 2017-03-20 | 2017-03-20 | A kind of UASB anaerobic reactors |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN206538255U (en) |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107572729A (en) * | 2017-10-21 | 2018-01-12 | 浙江千尧环境工程有限公司 | A kind of Waste Water Treatment of rubbish from cooking penetrating fluid |
| CN111115791A (en) * | 2020-01-04 | 2020-05-08 | 福建省晋蓝环保科技有限公司 | Ozone reaction tank for sewage treatment system |
| CN112794440A (en) * | 2020-12-29 | 2021-05-14 | 北京中电加美环保科技有限公司 | High-efficiency impact-resistant UASB reactor |
| CN113149206A (en) * | 2021-05-14 | 2021-07-23 | 郭梅兰 | Anaerobic reactor for wastewater treatment |
| CN113244699A (en) * | 2021-05-14 | 2021-08-13 | 兰州理工大学 | Design method of gas-liquid separator of EGSB reactor |
-
2017
- 2017-03-20 CN CN201720274171.2U patent/CN206538255U/en not_active Expired - Fee Related
Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107572729A (en) * | 2017-10-21 | 2018-01-12 | 浙江千尧环境工程有限公司 | A kind of Waste Water Treatment of rubbish from cooking penetrating fluid |
| CN111115791A (en) * | 2020-01-04 | 2020-05-08 | 福建省晋蓝环保科技有限公司 | Ozone reaction tank for sewage treatment system |
| CN111115791B (en) * | 2020-01-04 | 2021-11-26 | 福建省晋蓝环保科技有限公司 | Ozone reaction tank for sewage treatment system |
| CN112794440A (en) * | 2020-12-29 | 2021-05-14 | 北京中电加美环保科技有限公司 | High-efficiency impact-resistant UASB reactor |
| CN112794440B (en) * | 2020-12-29 | 2021-11-09 | 北京中电加美环保科技有限公司 | High-efficiency impact-resistant UASB reactor |
| CN113149206A (en) * | 2021-05-14 | 2021-07-23 | 郭梅兰 | Anaerobic reactor for wastewater treatment |
| CN113244699A (en) * | 2021-05-14 | 2021-08-13 | 兰州理工大学 | Design method of gas-liquid separator of EGSB reactor |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN206538255U (en) | A kind of UASB anaerobic reactors | |
| CN102120646B (en) | Efficient anaerobic biological tower reactor | |
| CN201330186Y (en) | High-efficiency integrated water purifying apparatus with helical sloping plate | |
| CN201952281U (en) | Cyclone type waste water treatment device of swell anaerobic sludge bed | |
| CN108298741B (en) | Oily sewage electric flocculation high-efficient purifier | |
| CN110526395A (en) | Eddy flow anaerobic reactor for waste water treatment system | |
| CN208166666U (en) | A kind of vortex self-circulating anaerobic reactor | |
| CN201132800Y (en) | Highly effective mixing upwash reactor for anaerobic solid | |
| CN210736319U (en) | Spiral-flow type anaerobic reactor | |
| CN202658004U (en) | Anaerobic reactor | |
| CN101973665B (en) | A/O reactor with functions of air lift, backflow as well as rotation and mixing of reflux | |
| CN208485667U (en) | A kind of multi-stage vortex self-circulating anaerobic reactor | |
| CN202284163U (en) | Anaerobic reactor | |
| CN201889100U (en) | Vertical-flow sewage sedimentation tank | |
| CN205099458U (en) | A modularization three -phase separator for UASB reactor | |
| CN110668570B (en) | High-efficiency granular sludge anaerobic tower reactor | |
| CN210457812U (en) | Multistage flocculation sewage treatment system based on magnetic powder recovery and distribution device | |
| CN206463554U (en) | A kind of high-efficiency swirl-type second pond | |
| CN209065527U (en) | A kind of expanded granular sludge bed reactor EGSB organic sewage treatment device | |
| CN201809222U (en) | A/O reactor of recirculating air lift and rotating mixed reflux | |
| CN206538286U (en) | A kind of integrated small displacement sewage water advanced treatment apparatus | |
| CN201354333Y (en) | Reactor for anaerobic granular sludge | |
| CN201020302Y (en) | Water treatment equipment | |
| CN217350899U (en) | Deep and wide-area aeration and precipitation integrated reactor | |
| CN204434358U (en) | A kind of flow lifting type anaerobe filter bed reactor |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CB03 | Change of inventor or designer information |
Inventor after: Yang Weihuan Inventor before: Yang Weihuan |
|
| CB03 | Change of inventor or designer information | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20190627 Address after: 311504 383 the Fuchun River Town Road, Tonglu, Hangzhou, Zhejiang Patentee after: Zhejiang run Cheng Environmental Protection Technology Co.,Ltd. Address before: 311504 206, two floor, 66 Li seven long street, the Fuchun River Town, Tonglu, Hangzhou, Zhejiang. Patentee before: ZHEJIANG WEIHUAN TECHNOLOGY CO.,LTD. |
|
| TR01 | Transfer of patent right | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20171003 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |