CN204939083U - A kind of eddy flow sludge classification anaerobic ammonia oxidation reactor - Google Patents
A kind of eddy flow sludge classification anaerobic ammonia oxidation reactor Download PDFInfo
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- CN204939083U CN204939083U CN201520735973.XU CN201520735973U CN204939083U CN 204939083 U CN204939083 U CN 204939083U CN 201520735973 U CN201520735973 U CN 201520735973U CN 204939083 U CN204939083 U CN 204939083U
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- Prior art keywords
- pipe
- mud
- sludge classification
- reaction chamber
- ammonia oxidation
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- 239000010802 sludge Substances 0.000 title claims abstract description 63
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 title claims abstract description 50
- 229910021529 ammonia Inorganic materials 0.000 title claims abstract description 25
- 230000003647 oxidation Effects 0.000 title claims abstract description 25
- 238000007254 oxidation reaction Methods 0.000 title claims abstract description 25
- 238000006243 chemical reaction Methods 0.000 claims abstract description 54
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 claims abstract description 46
- 238000010992 reflux Methods 0.000 claims abstract description 36
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 24
- 239000000377 silicon dioxide Substances 0.000 claims abstract description 23
- 230000001174 ascending effect Effects 0.000 claims abstract description 20
- 230000000630 rising effect Effects 0.000 claims abstract description 10
- 238000007599 discharging Methods 0.000 claims abstract description 8
- 239000012530 fluid Substances 0.000 claims description 3
- 238000007667 floating Methods 0.000 abstract description 3
- 238000000926 separation method Methods 0.000 abstract 1
- 239000007789 gas Substances 0.000 description 9
- 239000002351 wastewater Substances 0.000 description 6
- 238000000034 method Methods 0.000 description 4
- 239000008187 granular material Substances 0.000 description 3
- 239000007788 liquid Substances 0.000 description 3
- 229910002651 NO3 Inorganic materials 0.000 description 2
- NHNBFGGVMKEFGY-UHFFFAOYSA-N Nitrate Chemical compound [O-][N+]([O-])=O NHNBFGGVMKEFGY-UHFFFAOYSA-N 0.000 description 2
- XKMRRTOUMJRJIA-UHFFFAOYSA-N ammonia nh3 Chemical compound N.N XKMRRTOUMJRJIA-UHFFFAOYSA-N 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- QGZKDVFQNNGYKY-UHFFFAOYSA-O Ammonium Chemical compound [NH4+] QGZKDVFQNNGYKY-UHFFFAOYSA-O 0.000 description 1
- 239000002028 Biomass Substances 0.000 description 1
- IOVCWXUNBOPUCH-UHFFFAOYSA-M Nitrite anion Chemical compound [O-]N=O IOVCWXUNBOPUCH-UHFFFAOYSA-M 0.000 description 1
- JVMRPSJZNHXORP-UHFFFAOYSA-N ON=O.ON=O.ON=O.N Chemical compound ON=O.ON=O.ON=O.N JVMRPSJZNHXORP-UHFFFAOYSA-N 0.000 description 1
- 229910000831 Steel Inorganic materials 0.000 description 1
- 230000004888 barrier function Effects 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 239000003653 coastal water Substances 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 239000011521 glass Substances 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- QJGQUHMNIGDVPM-UHFFFAOYSA-N nitrogen group Chemical group [N] QJGQUHMNIGDVPM-UHFFFAOYSA-N 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
- 238000001556 precipitation Methods 0.000 description 1
- 238000007789 sealing Methods 0.000 description 1
- 239000010959 steel Substances 0.000 description 1
Landscapes
- Treatment Of Sludge (AREA)
Abstract
The utility model discloses a kind of eddy flow sludge classification anaerobic ammonia oxidation reactor, reactor body establishes mixing zone, Anammox reaction zone, settling region and cyclone classification district from top to bottom successively.Bottom mud discharging mouth, cyclone water distributor, water inlet pipe and refluxing opening are established in mixing zone; Anammox reaction chamber and mud downtake are established in Anammox reaction zone, and Anammox reaction zone is connected by airtight transverse wall with settling region, symmetrical ascending current pipe and mud internal reflux pipe on transverse wall; Shore pipe, settling chamber, refluxing opening, overflow weir and rising pipe are established in settling region; Cyclone classification district establishes scum silica frost surge drum and scum pipe, and sludge classification device, feed-pipe, upflow tube and mud downtake are established in scum silica frost surge drum inside.The utility model utilizes the effective fractional separation scum silica frost of the cyclonic action of sludge classification device, floating sludge and can settled sludge, and structure is simple, and space is taken up an area little, and utilize self aerogenesis lift, without the need to external impetus, fractional efficiency is high, can maintain the stability of reactor.
Description
Technical field
The utility model relates to a kind of anaerobic ammonia oxidation reactor, particularly relates to a kind of eddy flow sludge classification anaerobic ammonia oxidation reactor.
Background technology
Nitrate pollution aggravation is water body large-scale outbreak wawter bloom and the Chi Chao Alto major incentive such as China lake, river and coastal waters.Wastewater biological denitrificaion is the important means that waste water nitrate pollution controls.
Anammox denitrogenation is a kind of novel biological dinitrification technology grown up the nineties in last century, and it take ammonia as electron donor, and nitrite is electron acceptor(EA), produces N
2.Anaerobic ammonia oxidation process without the need to organism, can energy efficient and running cost.Anaerobic ammonia oxidation process has been used successfully to the high ammonia-nitrogen wastewaters such as treating refuse percolate, gourmet powder waste water, piggery wastewater, sludge-digestion liquid, Be very effective.
Anammox is anaerobic reaction, conventional anaerobic reactor.But research and apply finds, anaerobic ammonia oxidation process also has its intrinsic defect.Under high loads, a large amount of granule sludge floats (inner aerogenesis, density reduces) on the one hand, causes mud seriously to run off; Inside reactor scum silica frost can not be cleared up in time on the other hand, and easy barrier gas passage, causes operation troubles.For this reason, the utility model devises a kind of eddy flow sludge classification anaerobic ammonia oxidation reactor, to be separated floating sludge, returns settled sludge, maintains the biomass needed for reactor operation, is discharged by scum silica frost in reactor simultaneously, ensures that reactor normally runs.
Summary of the invention
The purpose of this utility model overcomes the deficiencies in the prior art, provides eddy flow sludge classification anaerobic ammonia oxidation reactor.Concrete technical scheme is as follows:
Anaerobic ammonia oxidation reactor comprises mud discharging mouth, cyclone water distributor, water inlet pipe, refluxing opening, reaction chamber, mud downtake, ascending current pipe, mud internal reflux pipe, airtight transverse wall, shore pipe, settling chamber, feed-pipe, sludge classification device, upflow tube, overflow weir, rising pipe, scum silica frost surge drum, scum pipe and valve.
Reactor body arranges airtight connected settling chamber and reaction chamber from top to bottom, separated by airtight transverse wall between settling chamber and reaction chamber, transverse wall is symmetrically arranged with ascending current pipe and mud internal reflux pipe, and the bottom of mud internal reflux pipe is lower than the bottom of ascending current pipe;
Reaction chamber bottom centre is provided with mud discharging mouth, and lower sides is provided with water inlet pipe and refluxing opening; Reaction chamber inner bottom part installs the cyclone water distributor be connected with water inlet pipe;
Settling chamber's lower case diameter convergent from top to bottom, its sloped sidewall is provided with shore pipe; In the middle part of settling chamber, outer wall is provided with refluxing opening, and external wall of upper portion is provided with overflow weir and rising pipe;
Sludge classification device is arranged on the central shaft of settling chamber, and its underpart is hollow cone, and cone top is higher than overflow weir; Sludge classification device top is provided with upflow tube, and sidewall is connected with feed-pipe, and feed-pipe lower end communicates with reactor top; Be connected with mud downtake bottom sludge classification device, mud downtake arrives above refluxing opening through airtight transverse wall; Be provided with scum silica frost surge drum outside sludge classification device, cylinder slanted floor, lowest part is connected with scum pipe, and scum pipe arranges valve.
As preferably: the inclination alpha of described settling chamber's lower sides is 45 °; The angle γ of scum silica frost surge drum bottom surface and sidewall is 100 °; The cone angle beta of sludge classification device bottom centrum is 20 °, to ensure good gradation rate.
As preferably: described reaction chamber aspect ratio is 8 ~ 10:1, to ensure to produce enough gas lifting force.
As preferably: described ascending current pipe diameter and reaction chamber diameter ratio are 1:6 ~ 12, and the length ratio of ascending current pipe in reaction chamber and settling chamber is 2 ~ 8:1.
As preferably: described mud internal reflux pipe diameter and reaction chamber diameter ratio are 1:6 ~ 12, and the length ratio of mud internal reflux pipe in reaction chamber and settling chamber is 1:2 ~ 8.
As preferably: described sludge classification device upper diameter and reaction chamber diameter ratio are 1:4 ~ 6.
As preferably: described sludge classification device upper diameter and scum silica frost surge drum diameter ratio are 1:4 ~ 6.
As preferably: the opening for feed of described feed-pipe is higher than overflow weir top 0.2 ~ 1.2m.
As preferably: described feed-pipe and mud downtake diameter are 100mm, to ensure the flow rate that fluid is certain.Overfall tube diameter is 50mm.
Compared with prior art, the beneficial effects of the utility model are: 1) sludge classification device is established on top, settling region, and internal recycle conduit is established in bottom, simple compared to triphase separator structure, take up room little; 2) utilize self aerogenesis of reaction as the lifting power of material, tangentially enter sludge classification device, without the need to external impetus; 3) utilize eddy flow to the separating effect of granule sludge, make to return to mixing zone along mud downtake by settled sludge, gas, ascending liquid and floating sludge are derived by top upflow tube; 4) sludge classification device fractional efficiency is high, and with gas and liquid for medium, the difference according to sludge density and granular size carries out classification disposal.
Accompanying drawing explanation
Fig. 1 is a kind of eddy flow sludge classification anaerobic ammonia oxidation reactor section of structure;
Fig. 2 is a kind of eddy flow sludge classification anaerobic ammonia oxidation reactor structure vertical view;
In figure: mixing zone I, Anammox reaction zone II, settling region III, cyclone classification district IV; Bottom mud discharging mouth 1, cyclone water distributor 2, water inlet pipe 3, refluxing opening 4, reaction chamber 5, mud downtake 6, ascending current pipe 7, mud internal reflux pipe 8, sealing transverse wall 9, shore pipe 10, settling chamber 11, feed-pipe 12, sludge classification device 13, upflow tube 14, overflow weir 15, rising pipe 16, scum silica frost surge drum 17, scum pipe 18, residual cake valve 19.
Embodiment
Below in conjunction with concrete the drawings and specific embodiments, the utility model is described further.If there is no specified otherwise or conflict between each preferred implementation, arbitrary combination can be carried out.
As shown in Figure 1, 2, eddy flow sludge classification anaerobic ammonia oxidation reactor, reactor monolith is divided into mixing zone I, Anammox reaction zone II, settling region III and cyclone classification district IV; Specifically comprise mud discharging mouth 1, cyclone water distributor 2, water inlet pipe 3, refluxing opening 4, reaction chamber 5, mud downtake 6, ascending current pipe 7, mud internal reflux pipe 8, airtight transverse wall 9, shore pipe 10, settling chamber 11, feed-pipe 12, sludge classification device 13, upflow tube 14, overflow weir 15, rising pipe 16, scum silica frost surge drum 17, scum pipe 18 and valve 19.
Reactor body arranges airtight connected settling chamber 11 and reaction chamber 5 from top to bottom, separated by airtight transverse wall 9 between settling chamber 11 and reaction chamber 5, on transverse wall 9, the right and left is symmetrically arranged with ascending current pipe 7 and mud internal reflux pipe 8, and two pipes all stretch out airtight transverse wall 9 certain distance up and down, and the residing height in the bottom of mud internal reflux pipe 8 lower than ascending current pipe 7 bottom residing for height.
Reaction chamber 5 bottom centre is provided with mud discharging mouth 1, for the mud by discharge precipitation.Reaction chamber 5 lower sides is provided with water inlet pipe 3 and refluxing opening 4; Reaction chamber 5 inner bottom part installs the cyclone water distributor 2 be connected with water inlet pipe 3.
Settling chamber 11 lower case diameter convergent from top to bottom, in rounding tower, its sloped sidewall is provided with shore pipe 10; In the middle part of settling chamber 11, outer wall is provided with refluxing opening 4, and this refluxing opening communicates with the refluxing opening of reaction chamber bottom, as return line.Reaction chamber 5 external wall of upper portion is provided with overflow weir 15 and rising pipe 16, and overflow weir 15 water outlet is discharged by rising pipe 16.
Sludge classification device 13 is arranged on the central shaft of settling chamber 11, and its underpart is hollow cone, and top is straight-tube shape, and cone top is higher than overflow weir 15.Sludge classification device 13 top is provided with upflow tube 14, for Exhaust Gas and scum silica frost.Sludge classification device 13 sidewall is connected with feed-pipe 12, and feed-pipe 12 lower end communicates with reaction chamber 5 top but do not stretch in reaction chamber 5.Be connected with mud downtake 6 bottom sludge classification device 13, mud downtake 6 is vertically arranged, and arrives above refluxing opening 4 through airtight transverse wall 9; Be provided with scum silica frost surge drum 17 outside sludge classification device 13, cylinder slanted floor, near lowest part, be connected with scum pipe 18, scum pipe 18 is arranged valve 19, for controlling opening and closing.
As a kind of preferred implementation: the inclination alpha of described settling chamber 11 lower sides is 45 °; The angle γ of scum silica frost surge drum 17 bottom surface and sidewall is 100 °; The cone angle beta of sludge classification device 13 bottom centrum is 20 °.Device under these angles, has good gradation rate.
As a kind of preferred implementation: described reaction chamber 5 aspect ratio is 8 ~ 10:1, to ensure to produce enough gas lifting force.
As a kind of preferred implementation: described ascending current pipe 7 diameter and reaction chamber 5 diameter ratio are 1:6 ~ 12, ascending current pipe 7 is in Anammox reaction zone II and settling region III(and reaction chamber 5 and settling chamber 11) in length ratio be 2 ~ 8:1.
As a kind of preferred implementation: described mud internal reflux pipe 8 diameter and reaction chamber 5 diameter ratio are 1:6 ~ 12, mud internal reflux pipe 8 is in Anammox reaction zone II and settling region III(and reaction chamber 5 and settling chamber 11) in length ratio be 1:2 ~ 8.
As a kind of preferred implementation: described sludge classification device 13 upper diameter and reaction chamber 5 diameter ratio are 1:4 ~ 6.
As a kind of preferred implementation: described sludge classification device 13 upper diameter and scum silica frost surge drum 17 diameter ratio are 1:4 ~ 6.
As a kind of preferred implementation: the opening for feed of described feed-pipe 12 is higher than overflow weir 15 top 0.2 ~ 1.2m.
As a kind of preferred implementation: described feed-pipe 12 is 100mm, to ensure the flow rate that fluid is certain with mud downtake 6 diameter.Upflow tube 14 diameter is 50mm.
Eddy flow sludge classification anaerobic ammonia oxidation reactor can make of synthetic glass or steel plate, its working process is as follows: flowed into by water inlet pipe 3 containing ammonia nitrogen and nitrite nitrogen waste water, upwards reactor is entered through cyclone water distributor 2, with mixed by the phegma of refluxing opening 4 and the returned sluge of mud downtake 6 after enter the reaction chamber 5 of Anammox reaction zone II, after nitrogenous effluent mixes with anaerobic ammonium oxidation granular sludge, ascending current enters settling region by ascending current pipe 7, and settling region partial sludge returns reaction chamber 5 through mud internal reflux pipe 8 and mixes.The gas collection that reaction chamber 5 produces is in top, under raising force effect, gas carries granule sludge and scum silica frost promotes through feed-pipe 12, tangentially enter sludge classification device 13, after cyclonic action, partial particulate mud returns to mixing zone I by mud downtake 6 flow by gravity, gas and scum silica frost are upwards discharged through upflow tube 14, scum silica frost deposits in scum silica frost surge drum 17, after assembling some amount, opens residual cake valve 19 emptying by scum pipe 18.Settling chamber 11 water flow inside is then discharged by rising pipe 16 through overflow weir 15.
Claims (9)
1. an eddy flow sludge classification anaerobic ammonia oxidation reactor, is characterized in that: reactor comprises mud discharging mouth (1), cyclone water distributor (2), water inlet pipe (3), refluxing opening (4), reaction chamber (5), mud downtake (6), ascending current pipe (7), mud internal reflux pipe (8), airtight transverse wall (9), shore pipe (10), settling chamber (11), feed-pipe (12), sludge classification device (13), upflow tube (14), overflow weir (15), rising pipe (16), scum silica frost surge drum (17), scum pipe (18) and valve (19);
Reactor body arranges airtight connected settling chamber (11) and reaction chamber (5) from top to bottom, separated by airtight transverse wall (9) between settling chamber (11) and reaction chamber (5), transverse wall (9) is symmetrically arranged with ascending current pipe (7) and mud internal reflux pipe (8), and the bottom of mud internal reflux pipe (8) is lower than the bottom of ascending current pipe (7);
Reaction chamber (5) bottom centre is provided with mud discharging mouth (1), and lower sides is provided with water inlet pipe (3) and refluxing opening (4); Reaction chamber (5) inner bottom part installs the cyclone water distributor (2) be connected with water inlet pipe (3);
Settling chamber (11) lower case diameter convergent from top to bottom, its sloped sidewall is provided with shore pipe (10); Middle part, settling chamber (11) outer wall is provided with refluxing opening (4), and external wall of upper portion is provided with overflow weir (15) and rising pipe (16);
Sludge classification device (13) is arranged on the central shaft of settling chamber (11), and its underpart is hollow cone, and cone top is higher than overflow weir (15); Sludge classification device (13) top is provided with upflow tube (14), and sidewall is connected with feed-pipe (12), and feed-pipe (12) lower end communicates with reaction chamber (5) top; Sludge classification device (13) bottom is connected with mud downtake (6), and mud downtake (6) arrives refluxing opening (4) top through airtight transverse wall (9); Be provided with scum silica frost surge drum (17) outside sludge classification device (13), cylinder slanted floor, lowest part is connected with scum pipe (18), scum pipe (18) is arranged valve (19).
2. a kind of eddy flow sludge classification anaerobic ammonia oxidation reactor according to claim 1, is characterized in that: the inclination alpha of described settling chamber (11) lower sides is 45 °; The angle γ of scum silica frost surge drum (17) bottom surface and sidewall is 100 °; The cone angle beta of sludge classification device (13) bottom centrum is 20 °, to ensure good gradation rate.
3. a kind of eddy flow sludge classification anaerobic ammonia oxidation reactor according to claim 1, is characterized in that: described reaction chamber (5) aspect ratio is 8 ~ 10:1, to ensure to produce enough gas lifting force.
4. a kind of eddy flow sludge classification anaerobic ammonia oxidation reactor according to claim 1, it is characterized in that: described ascending current pipe (7) diameter and reaction chamber (5) diameter ratio are 1:6 ~ 12, the length ratio of ascending current pipe (7) part in reaction chamber (5) and settling chamber (11) is 2 ~ 8:1.
5. a kind of eddy flow sludge classification anaerobic ammonia oxidation reactor according to claim 1, it is characterized in that: described mud internal reflux pipe (8) diameter and reaction chamber (5) diameter ratio are 1:6 ~ 12, the length ratio of mud internal reflux pipe (8) part in reaction chamber (5) and settling chamber (11) is 1:2 ~ 8.
6. a kind of eddy flow sludge classification anaerobic ammonia oxidation reactor according to claim 1, is characterized in that: described sludge classification device (13) upper diameter and reaction chamber (5) diameter ratio are 1:4 ~ 6.
7. a kind of eddy flow sludge classification anaerobic ammonia oxidation reactor according to claim 1, is characterized in that: described sludge classification device (13) upper diameter and scum silica frost surge drum (17) diameter ratio are 1:4 ~ 6.
8. a kind of eddy flow sludge classification anaerobic ammonia oxidation reactor according to claim 1, is characterized in that: the opening for feed of described feed-pipe (12) is higher than overflow weir (15) top 0.2 ~ 1.2m.
9. a kind of eddy flow sludge classification anaerobic ammonia oxidation reactor according to claim 1, it is characterized in that: described feed-pipe (12) and mud downtake (6) diameter are 100mm, to ensure the flow rate that fluid is certain, upflow tube (14) diameter is 50mm.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520735973.XU CN204939083U (en) | 2015-09-22 | 2015-09-22 | A kind of eddy flow sludge classification anaerobic ammonia oxidation reactor |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520735973.XU CN204939083U (en) | 2015-09-22 | 2015-09-22 | A kind of eddy flow sludge classification anaerobic ammonia oxidation reactor |
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| Publication Number | Publication Date |
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| CN204939083U true CN204939083U (en) | 2016-01-06 |
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| CN201520735973.XU Withdrawn - After Issue CN204939083U (en) | 2015-09-22 | 2015-09-22 | A kind of eddy flow sludge classification anaerobic ammonia oxidation reactor |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105152324A (en) * | 2015-09-22 | 2015-12-16 | 浙江大学 | Anaerobic ammonia oxidation reactor capable of classifying sludge through cyclone |
| CN105906041A (en) * | 2016-06-07 | 2016-08-31 | 浙江大学 | Self-gas-flotation efficient anaerobic bioreactor and method thereof |
-
2015
- 2015-09-22 CN CN201520735973.XU patent/CN204939083U/en not_active Withdrawn - After Issue
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105152324A (en) * | 2015-09-22 | 2015-12-16 | 浙江大学 | Anaerobic ammonia oxidation reactor capable of classifying sludge through cyclone |
| CN105906041A (en) * | 2016-06-07 | 2016-08-31 | 浙江大学 | Self-gas-flotation efficient anaerobic bioreactor and method thereof |
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Legal Events
| Date | Code | Title | Description |
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| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| AV01 | Patent right actively abandoned | ||
| AV01 | Patent right actively abandoned |
Granted publication date: 20160106 Effective date of abandoning: 20170426 |