CN116022966B - Sewage total nitrogen removing device - Google Patents
Sewage total nitrogen removing device Download PDFInfo
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- CN116022966B CN116022966B CN202310051249.4A CN202310051249A CN116022966B CN 116022966 B CN116022966 B CN 116022966B CN 202310051249 A CN202310051249 A CN 202310051249A CN 116022966 B CN116022966 B CN 116022966B
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- 239000010865 sewage Substances 0.000 title claims abstract description 44
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 title claims abstract description 38
- 229910052757 nitrogen Inorganic materials 0.000 title claims abstract description 19
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 93
- 238000001914 filtration Methods 0.000 claims abstract description 72
- 238000006243 chemical reaction Methods 0.000 claims abstract description 30
- 238000011010 flushing procedure Methods 0.000 claims description 82
- 238000005273 aeration Methods 0.000 claims description 39
- 238000004062 sedimentation Methods 0.000 claims description 21
- 230000005540 biological transmission Effects 0.000 claims description 20
- 239000010802 sludge Substances 0.000 claims description 17
- 239000012528 membrane Substances 0.000 claims description 12
- 230000000712 assembly Effects 0.000 claims description 7
- 238000000429 assembly Methods 0.000 claims description 7
- 230000007306 turnover Effects 0.000 claims description 7
- 238000007790 scraping Methods 0.000 claims description 4
- 238000005276 aerator Methods 0.000 claims description 3
- 238000005452 bending Methods 0.000 claims description 2
- 239000002351 wastewater Substances 0.000 claims 2
- 230000009286 beneficial effect Effects 0.000 description 10
- 238000001556 precipitation Methods 0.000 description 6
- 238000000926 separation method Methods 0.000 description 5
- 239000007788 liquid Substances 0.000 description 3
- 230000000630 rising effect Effects 0.000 description 3
- 238000010586 diagram Methods 0.000 description 2
- 230000005484 gravity Effects 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- MMDJDBSEMBIJBB-UHFFFAOYSA-N [O-][N+]([O-])=O.[O-][N+]([O-])=O.[O-][N+]([O-])=O.[NH6+3] Chemical compound [O-][N+]([O-])=O.[O-][N+]([O-])=O.[O-][N+]([O-])=O.[NH6+3] MMDJDBSEMBIJBB-UHFFFAOYSA-N 0.000 description 1
- UEKDBDAWIKHROY-UHFFFAOYSA-L bis(4-bromo-2,6-ditert-butylphenoxy)-methylalumane Chemical compound [Al+2]C.CC(C)(C)C1=CC(Br)=CC(C(C)(C)C)=C1[O-].CC(C)(C)C1=CC(Br)=CC(C(C)(C)C)=C1[O-] UEKDBDAWIKHROY-UHFFFAOYSA-L 0.000 description 1
- 230000003111 delayed effect Effects 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 244000005700 microbiome Species 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 239000012466 permeate Substances 0.000 description 1
- 230000035484 reaction time Effects 0.000 description 1
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- 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
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W10/00—Technologies for wastewater treatment
- Y02W10/10—Biological treatment of water, waste water, or sewage
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- Purification Treatments By Anaerobic Or Anaerobic And Aerobic Bacteria Or Animals (AREA)
Abstract
The invention discloses a sewage total nitrogen removal device, which comprises a shell and further comprises: the integrated install in anaerobic zone, mixed reaction district and the filtration district that the intercommunication set up in the casing, mixed reaction district is connected with the filtration district through overflow subassembly, mixed reaction district is located anaerobic zone top, wash out water supply assembly install in the casing, and with anaerobic zone connects, wash out water supply assembly and be located filtration district top, water inlet and delivery port install in the casing surface, the water inlet with wash out water supply assembly and be connected, the delivery port is connected with the filtration district. The sewage total nitrogen removal device provided by the invention has the advantages of small occupied area, convenience in movement and strong applicability, and the anaerobic zone, the mixed reaction zone and the filtering zone are integrally arranged in the shell.
Description
Technical Field
The invention relates to the technical field of sewage treatment, in particular to a sewage total nitrogen removal device.
Background
Chinese patent CN114735903B discloses a device for removing total nitrogen from sewage and a method for operating the same, comprising: a denitrification tank, a precipitation separation zone and a supplementary reaction zone, wherein: the precipitation separation zone and the supplementary reaction zone are positioned in the denitrification tank, the precipitation separation zone is positioned above the supplementary reaction zone and is communicated with the supplementary reaction zone through a three-phase separator, sewage in the denitrification tank can flow into the supplementary reaction zone, and sewage subjected to nitrogen removal treatment in the precipitation zone can directly flow out of the denitrification tank; the top surface of the precipitation separation zone is sealed, the diameter of the top surface is larger than that of the bottom surface, and the interior of the supplementary reaction zone is filled with aerobic granular sludge; and an MABR membrane component is arranged in a space formed by the outer side wall of the precipitation separation area and the supplementary reaction area and the inner cavity of the denitrification tank, and the side wall of the denitrification tank is provided with an online COD detector and an online nitrate nitrogen detector. The device provided by the disclosure is simple in operation, saves energy consumption and has good water quality of effluent.
Along with the integrated development trend of the sewage treatment device, the sewage treatment device is required to have the advantages of small occupied area, convenient movement and strong applicability. The standby anaerobic tank and the denitrification tank of the sewage total nitrogen removal device are designed in a split mode, so that the occupied area of the device is slightly large, and the applicability is low.
Disclosure of Invention
In order to achieve the above purpose, the invention discloses a sewage total nitrogen removal device, which comprises a shell and further comprises: the integrated install in anaerobic zone, mixed reaction district and the filtration district that the intercommunication set up in the casing, mixed reaction district is connected with the filtration district through overflow subassembly, mixed reaction district is located anaerobic zone top, wash out water supply assembly install in the casing, and with anaerobic zone connects, wash out water supply assembly and be located filtration district top, water inlet and delivery port install in the casing surface, the water inlet with wash out water supply assembly and be connected, the delivery port is connected with the filtration district.
Preferably, the anaerobic zone is arranged in a bucket shape, and the water outlet end of the flushing water delivery assembly is attached to the inner wall of the anaerobic zone and extends to the bottom position in the anaerobic zone.
Preferably, a stirrer and anaerobic activated sludge are arranged in the anaerobic zone.
Preferably, the mixed reaction zone comprises:
the lower aeration zone is positioned above the anaerobic zone, the lower aeration zone is connected with the anaerobic zone through a three-phase separator, aerobic granular sludge is arranged in the lower aeration zone, and an aerator connected in the lower aeration zone is arranged on the surface of the shell;
the upper sedimentation zone is positioned above the lower aeration zone and is connected with the overflow assembly;
and the sloping plates are arranged in the lower aeration zone in parallel, and the aerobic granular sludge is attached to the surface of the sloping plates.
Preferably, the overflow assembly comprises:
the overflow groove is circumferentially arranged at a position close to the top of the inner wall of the upper sedimentation zone;
the overflow box is arranged at the side end of the upper sedimentation zone and connected with the overflow groove, and the overflow box is positioned in the flushing water delivery assembly;
the U-shaped overflow pipe, U-shaped overflow pipe one end stretches into wash out in the water supply subassembly, and with the overflow tank is connected, U-shaped overflow pipe other end stretches into in the filtration district, U-shaped overflow pipe is close to overflow tank end height and is greater than U-shaped overflow pipe is close to filtration district end height.
Preferably, the filtering area includes:
the water outlet is connected with the bottom water outlet area;
the top filtering area is positioned above the bottom water outlet area, an MBR filter membrane component is arranged in the top filtering area, and the other end of the U-shaped overflow pipe extends into the top filtering area and is positioned above the MBR filter membrane component;
the water filtering cap is arranged at the bottom in the top filtering area and is connected with the bottom water outlet area;
one end of the back flushing pipe penetrates through the shell and extends into the top filtering area from the top end of the top filtering area, and a back flushing valve is arranged at the other end of the back flushing pipe;
and the window is arranged on the surface of the shell and is connected with the top filtering area.
Preferably, the flushing water supply assembly comprises:
the upper flushing chamber is positioned above the filtering area, the water inlet is connected with the upper flushing chamber, and the bottom of the upper flushing chamber is arranged in a downward inclined mode;
one end of the lower flushing pipe is connected with the bottom end of the upper flushing chamber, and the other end of the lower flushing pipe is attached to the inner wall of the anaerobic zone and extends to the bottom position in the anaerobic zone.
Preferably, the mixed reaction zone further comprises:
the upper outlets are arranged at the top part in the lower aeration zone and are communicated with the upper sedimentation zone, and the upper outlets are arranged in a strip shape;
the baffle plate assemblies are positioned between the two upper outlets, and the two baffle plate assemblies are slidably arranged at the inner top of the lower aeration zone and are arranged in one-to-one correspondence to the upper outlets;
the transverse sliding column is positioned between the two inclined plates, is connected to the inner top of the lower aeration zone in a sliding manner and is positioned between the two baffle plate assemblies;
the driving roller is arranged on the transverse sliding column and is used for driving the baffle plate assembly to slide;
the scraping plate is attached to the surface of the inclined plate and is arranged on the transverse sliding column through a bracket;
and the flushing component is arranged on the inner wall of the upper flushing chamber and is connected with the transverse sliding column.
Preferably, the baffle assembly includes:
a baffle plate, which can cover the upper outlet;
the arc-shaped slideway is arranged at the end, close to the transverse sliding strut, of the baffle plate, and the driving roller is connected to the arc-shaped slideway in a sliding manner;
the limiting sliding sleeves are arranged at two ends of the baffle in the length direction;
the limiting cross rod is fixedly arranged at the inner top of the lower aeration zone, the limiting sliding sleeve is sleeved on the limiting cross rod, and the reset spring is sleeved on the limiting cross rod and abuts against the limiting sliding sleeve.
Preferably, the flushing assembly comprises:
the supporting seat is fixedly arranged on the inner wall of the upper flushing chamber;
the overturning rod is bent at an obtuse angle and hinged to the bottom end of the supporting seat through a mounting shaft, the flushing plate is mounted on the overturning rod, and a reset torsion spring is sleeved on the mounting shaft;
the transmission chute is arranged on the turning rod;
one end of the transmission cross rod extends into the lower aeration zone and is connected with the transverse sliding column, and the other end of the transmission cross rod extends into the upper flushing chamber;
the limiting slide block is connected in the transmission chute in a sliding manner, and is connected with the other end of the transmission cross rod.
Drawings
In order to more clearly illustrate the embodiments of the present invention or the technical solutions in the prior art, the drawings that are needed in the description of the embodiments or the prior art will be briefly described, and it is obvious that the drawings in the description below are some embodiments of the present invention, and other drawings can be obtained according to the drawings without inventive effort for a person skilled in the art.
FIG. 1 is a schematic diagram of a first embodiment of the present invention;
FIG. 2 is a second schematic diagram of the structure of the present invention;
fig. 3 is an enlarged view of reference a in fig. 2;
FIG. 4 is a schematic view of the swash plate structure of the present invention;
fig. 5 is a schematic view of a baffle assembly according to the present invention.
In the figure: 10. a housing; 11. a water inlet; 12. a water outlet; 2. an anaerobic zone; 21. a stirrer; 3. a mixing reaction zone; 31. a lower aeration zone; 32. an upper sedimentation zone; 33. a sloping plate; 34. an upper outlet; 35. a baffle assembly; 36. a traversing slide column; 37. driving the roller; 38. a scraper; 39. flushing the assembly; 4. a filtration zone; 41. a bottom water outlet area; 42. a top filtration zone; 43. a water filtering cap; 44. a back flushing pipe; 45. a backwash valve; 5. an overflow assembly; 51. an overflow trough; 52. an overflow box; a U-shaped overflow tube; 6. flushing the water delivery assembly; 61. an upper flush chamber; 62. a lower flushing pipe; 63. flushing the plate; 71. a baffle; 72. an arc-shaped slideway; 73. a limit sliding sleeve; 74. a limiting cross bar; 75. a return spring; 76. turning over the rod; 77. a transmission chute; 78. a transmission cross bar; 79. a limit sliding block; 70. and a supporting seat.
Detailed Description
The following description of the embodiments of the present invention will be made apparent and fully in view of the accompanying drawings, in which some, but not all embodiments of the invention are shown. All other embodiments, which can be made by those skilled in the art based on the embodiments of the invention without making any inventive effort, are intended to be within the scope of the invention.
Examples
The invention will be further described with reference to the accompanying drawings.
As shown in fig. 1 to 5, the apparatus for removing total nitrogen from sewage provided in this embodiment includes a housing 10, and further includes: the integrated install in anaerobic zone 2, mixed reaction zone 3 and the filtration district 4 that the intercommunication set up in casing 10, mixed reaction zone 3 is connected with filtration district 4 through overflow subassembly 5, mixed reaction zone 3 is located anaerobic zone 2 top, wash out water supply assembly 6 install in casing 10, and with anaerobic zone 2 connects, wash out water supply assembly 6 is located filtration district 4 top, water inlet 11 and delivery port 12 install in casing 10 surface, water inlet 11 with wash out water supply assembly 6 and be connected, delivery port 12 is connected with filtration district 4.
The working principle and beneficial effects of the technical scheme are as follows:
the invention discloses a total nitrogen removal device for sewage, wherein the sewage is sent into a flushing water delivery assembly 6 from a water inlet 11, the sewage is flushed into an anaerobic zone 2 under the slope assistance of the flushing water delivery assembly 6, overflows into a mixed reaction zone 3 communicated with the anaerobic zone 2, overflows into a filtering zone 4 communicated with the mixed reaction zone 3 through an overflow assembly 5, and filtered water is discharged from a water outlet 12. The sewage total nitrogen removal device provided by the invention has the advantages of small occupied area, convenience in movement and strong applicability, and the anaerobic zone 2, the mixed reaction zone 3 and the filtering zone 4 are integrally arranged in the shell 10.
In one embodiment, the anaerobic zone 2 is arranged in a bucket shape, and the water outlet end of the flushing water delivery assembly 6 is abutted against the inner wall of the anaerobic zone 2 and extends to the bottom position in the anaerobic zone 2.
The working principle and beneficial effects of the technical scheme are as follows:
under the slope assistance of the flushing water delivery assembly 6, sewage is flushed into the anaerobic zone 2, and the sewage is flushed into the bottom of the anaerobic zone 2 from the water outlet end of the flushing water delivery assembly 6, so that the activated sludge is prevented from accumulating in the bottom of the anaerobic zone 2, and the mobility of the activated sludge in the anaerobic zone 2 is maintained.
In one embodiment, the anaerobic zone 2 is provided with a stirrer 21 and anaerobic activated sludge.
The beneficial effects of the technical scheme are as follows:
the arrangement of the stirrer 21 improves the fluidity of the anaerobic activated sludge in the anaerobic zone 2 and prevents the anaerobic activated sludge from accumulating at the bottom of the anaerobic zone 2.
In one embodiment, the mixed reaction zone 3 comprises:
the lower aeration zone 31 is positioned above the anaerobic zone 2, the lower aeration zone 31 is connected with the anaerobic zone 2 through a three-phase separator, aerobic granular sludge is arranged in the lower aeration zone 31, and an aerator connected in the lower aeration zone 31 is arranged on the surface of the shell 10;
an upper sedimentation zone 32, wherein the upper sedimentation zone 32 is positioned above the lower aeration zone 31, and the upper sedimentation zone 32 is connected with the overflow assembly 5;
and a sloping plate 33, wherein a plurality of sloping plates 33 are arranged in parallel in the lower aeration zone 31, and the aerobic granular sludge is attached to the surface of the sloping plate 33.
The working principle and beneficial effects of the technical scheme are as follows:
sewage in the anaerobic zone 2 overflows into a lower aeration zone 31 communicated with the sewage through a three-phase separator, after the aerobic granular sludge attached to the surface of the inclined plate 33 and sewage are degraded by microorganisms, the sewage overflows into an upper sedimentation zone 32 communicated with the lower aeration zone 31, and along with the rising of the liquid level in the upper sedimentation zone 32, the water is sent into a filtering zone 4 for filtering through the self-overflow assembly 5.
In one embodiment, the overflow assembly 5 comprises:
an overflow groove 51, wherein the overflow groove 51 is circumferentially arranged at a position close to the top of the inner wall of the upper sedimentation zone 32;
an overflow tank 52, wherein the overflow tank 52 is installed at the side end of the upper sedimentation zone 32 and connected with the overflow groove 51, and the overflow tank 52 is positioned in the flushing water supply assembly 6;
the U-shaped overflow pipe 53, U-shaped overflow pipe 53 one end stretches into wash water supply assembly 6, and with overflow box 52 is connected, U-shaped overflow pipe 53 other end stretches into in the filtration district 4, U-shaped overflow pipe 53 is close to overflow box 52 end height more than U-shaped overflow pipe 53 is close to filtration district 4 end height.
The working principle and beneficial effects of the technical scheme are as follows:
along with the rising of the liquid level in the upper sedimentation zone 32, the water after aeration sedimentation overflows into the overflow groove 51 and flows into the overflow box 52 communicated with the overflow groove 51, the height of the U-shaped overflow pipe 53 close to the overflow box 52 is larger than that of the U-shaped overflow pipe 53 close to the filtering zone 4, and under the gravity of the water, the water is flushed into the filtering zone 4 to finish filtering, and then is discharged from the water outlet 12.
In one embodiment, the filtering section 4 comprises:
a bottom water outlet area 41, wherein the water outlet 12 is connected with the bottom water outlet area 41;
the top filtering area 42 is positioned above the bottom water outlet area 41, an MBR filter membrane component is arranged in the top filtering area 42, and the other end of the U-shaped overflow pipe 53 extends into the top filtering area 42 and is positioned above the MBR filter membrane component;
a water filtering cap 43, wherein the water filtering cap 43 is installed at the bottom of the top filtering area 42 and is connected with the bottom water outlet area 41;
a back flushing pipe 44, wherein one end of the back flushing pipe 44 penetrates through the shell 10 and extends into the top filtering area 42 from the top end of the top filtering area 42, and a back flushing valve 45 is arranged at the other end of the back flushing pipe 44;
a window mounted to the surface of the housing 10 and connected to the top filter section 42.
The working principle and beneficial effects of the technical scheme are as follows:
the water is sent into the top filtering area 42 from the U-shaped overflow pipe 53, the water falls under the action of gravity, the MBR filter membrane assembly installed in the top filtering area 42 completes the filtration of sewage, the filtered water is collected into the bottom water outlet area 41 from the water filtering cap 43 and finally discharged from the water outlet 12, along with the increase of the filter materials attached to the surface of the MBR filter membrane assembly, the water cannot permeate into the bottom of the top filtering area 42, along with the rising of the liquid level in the top filtering area 42, the water overflows into the backwash pipe 44, the backwash valve 45 is opened, the water in the top filtering area 42 is flushed out, and the filter materials attached to the surface of the MBR filter membrane assembly are taken away, so that the water sent out by the U-shaped overflow pipe 53 is filtered under the action of the MBR filter membrane assembly after the MBR filter membrane assembly resumes the filtration capacity.
In one embodiment, the flush water supply assembly 6 comprises:
the upper flushing chamber 61 is positioned above the filtering area 4, the water inlet 11 is connected with the upper flushing chamber 61, and the bottom in the upper flushing chamber 61 is arranged in a lower inclined mode;
one end of the lower flushing pipe 62 is connected with the bottom end of the upper flushing chamber 61, and the other end of the lower flushing pipe 62 is abutted against the inner wall of the anaerobic zone 2 and extends to the bottom position in the anaerobic zone 2.
The working principle and beneficial effects of the technical scheme are as follows:
sewage is fed into the upper flushing chamber 61 from the water inlet 11, and the bottom in the upper flushing chamber 61 is arranged in a downward inclined manner, so that the sewage is flushed into the bottom in the anaerobic zone 2 from the lower flushing pipe 62 under the slope assistance of the upper flushing chamber 61, and anaerobic activated sludge is prevented from accumulating in the bottom in the anaerobic zone 2.
In one example, the mixed reaction zone 3 further comprises:
an upper outlet 34, wherein two upper outlets 34 are arranged at the top in the lower aeration zone 31 and are communicated with the upper sedimentation zone 32, and the upper outlets 34 are arranged in a strip shape;
the baffle plate assemblies 35 are positioned between the two upper outlets 34, and the two baffle plate assemblies 35 are slidably arranged at the top in the lower aeration zone 31 and are arranged in one-to-one correspondence with the upper outlets 34;
a traversing slide column 36, wherein the traversing slide column 36 is positioned between the two inclined plates 33, and the traversing slide column 36 is connected to the inner top of the lower aeration zone 31 in a sliding way and positioned between the two baffle assemblies 35;
a driving roller 37, wherein the driving roller 37 is mounted on the traverse slide column 36, and the driving roller 37 is used for driving the baffle assembly 35 to slide;
a scraper 38, wherein the scraper 38 is abutted against the surface of the inclined plate 33, and the scraper 38 is mounted on the traversing slide column 36 through a bracket;
a flushing assembly 39, said flushing assembly 39 is mounted on the inner wall of the upper flushing chamber 61, said flushing assembly 39 is connected with the traverse slide 36.
The working principle and beneficial effects of the technical scheme are as follows:
sewage is fed into the upper flushing chamber 61 from the water inlet 11, and is flushed into the inner bottom of the anaerobic zone 2 from the lower flushing pipe 62 along the slope of the upper flushing chamber 61, when the sewage water flow is large in stages, the sewage is impacted on the flushing component 39 and is quickly flushed into the anaerobic zone 2, at the moment, the sewage in the anaerobic zone 2 overflows into the lower aeration zone 31 at too high speed, the flushing component 39 drives the traversing slide column 36 to slide at the inner top of the lower aeration zone 31, when the traversing slide column 36 slides between two adjacent inclined plates 33, the baffle component 35 is driven to slide through the driving roller 37 arranged on the traversing slide column 36, and the baffle component 35 synchronously drives the scraping plate 38 to scrape the surface of the inclined plate 33 when the upper outlet 34 is blocked, so that the activity of aerobic granular sludge attached to the surface of the inclined plate 33 is improved, and meanwhile, the time that the sewage overflows into the upper sedimentation zone 32 from the water inlet 11 is delayed, and the full reaction time of the sewage is given. When the sewage flow is restored to normal, the sewage cannot impact on the flushing assembly 39, and the traverse slide 36 does not act.
In one embodiment the baffle assembly 35 comprises:
a baffle 71, said baffle 71 being capable of covering said upper outlet 34;
the arc-shaped slideway 72 is arranged at the end of the baffle 71 close to the sideslip slide column 36, and the driving roller 37 is connected to the arc-shaped slideway 72 in a sliding way;
a limiting sliding sleeve 73, wherein the limiting sliding sleeve 73 is arranged at two ends of the baffle 71 in the length direction;
the limiting cross rod 74, the limiting cross rod 74 is fixedly installed at the inner top of the lower aeration zone 31, the limiting sliding sleeve 73 is sleeved on the limiting cross rod 74, and the reset spring 75 is sleeved on the limiting cross rod 74 and is propped against the limiting sliding sleeve 73.
The working principle and beneficial effects of the technical scheme are as follows:
when the traverse slide column 36 slides between the two adjacent inclined plates 33, the driving roller 37 arranged on the traverse slide column 36 slides on the arc-shaped slideway 72, so that the baffle 71 and the limit sliding sleeve 73 connected with the baffle 71 are driven to move along the shrinkage direction of the limit cross rod 74 to the reset spring 75, the baffle 71 finishes covering the upper outlet 34, and when sewage cannot impact on the flushing assembly 39, the traverse slide column 36 drives the driving roller 37 to be separated from the arc-shaped slideway 72, the reset spring 75 drives the limit sliding sleeve 73 to reset on the limit cross rod 74, and the baffle 71 releases covering of the upper outlet 34 again.
In one embodiment, the flush assembly 39 includes:
the supporting seat 70 is fixedly arranged on the inner wall of the upper flushing chamber 61;
the overturning rod 76 is arranged in an obtuse angle bending way, the overturning rod 76 is hinged to the bottom end of the supporting seat 70 through a mounting shaft, the flushing plate 63 is mounted on the overturning rod 76, and a reset torsion spring is sleeved on the mounting shaft;
the transmission chute 77 is arranged on the turnover rod 76;
a transmission cross rod 78, wherein one end of the transmission cross rod 78 extends into the lower aeration zone 31 and is connected with the traverse sliding column 36, and the other end of the transmission cross rod 78 extends into the upper flushing chamber 61;
the limiting slide block 79 is slidably connected in the transmission chute 77, and the limiting slide block 79 is connected with the other end of the transmission cross rod 78.
The working principle and beneficial effects of the technical scheme are as follows:
when the sewage water flow is large in stages, the sewage impacts on the flushing plate 63, so that the turnover rod 76 connected with the flushing plate 63 is driven to turn downwards on the supporting seat 70 by taking the installation shaft as the center, under the cooperation of the limit sliding block 79 and the transmission sliding groove 77, the transmission cross rod 78 is driven to extend into the lower aeration zone 31, so that the transverse sliding column 36 is driven to slide, and when the sewage does not impact on the flushing plate 63, the turnover rod 76 is lifted again under the action of the reset torsion spring to complete reset.
It is apparent that the above examples are given by way of illustration only and are not limiting of the embodiments. Other variations or modifications of the above teachings will be apparent to those of ordinary skill in the art. It is not necessary here nor is it exhaustive of all embodiments. While still being apparent from variations or modifications that may be made by those skilled in the art are within the scope of the invention.
Claims (7)
1. A total nitrogen removal device for wastewater, comprising a housing (10), characterized in that it further comprises: the device is characterized by comprising an anaerobic zone (2), a mixed reaction zone (3) and a filtering zone (4) which are integrally arranged in a shell (10) and are communicated, wherein the mixed reaction zone (3) is connected with the filtering zone (4) through an overflow assembly (5), the mixed reaction zone (3) is positioned above the anaerobic zone (2), a flushing water supply assembly (6) is arranged in the shell (10) and is connected with the anaerobic zone (2), the flushing water supply assembly (6) is positioned above the filtering zone (4), a water inlet (11) and a water outlet (12) are arranged on the surface of the shell (10), the water inlet (11) is connected with the flushing water supply assembly (6), and the water outlet (12) is connected with the filtering zone (4);
the mixed reaction zone (3) comprises: the lower aeration zone (31) is positioned above the anaerobic zone (2), the lower aeration zone (31) is connected with the anaerobic zone (2) through a three-phase separator, aerobic granular sludge is arranged in the lower aeration zone (31), an aerator connected in the lower aeration zone (31) is arranged on the surface of the shell (10), the upper sedimentation zone (32) is positioned above the lower aeration zone (31), the upper sedimentation zone (32) is connected with the overflow assembly (5), a plurality of inclined plates (33) are arranged in the lower aeration zone (31) in parallel, and the aerobic granular sludge is attached to the surface of the inclined plates (33);
the mixed reaction zone (3) further comprises: the device comprises two upper outlets (34) which are arranged at the inner top of a lower aeration zone (31) and are communicated with the upper sedimentation zone (32), a baffle assembly (35) is arranged between the two upper outlets (34), a transverse sliding column (36) is arranged between two inclined plates (33), the transverse sliding column (36) is slidably connected to the inner top of the lower aeration zone (31) and is arranged between the two baffle assemblies (35), a driving roller (37) is arranged on the transverse sliding column (36), a scraping plate (38) is attached to the surface of the inclined plate (33), the scraping plate (38) is arranged on the transverse sliding column (36) through a bracket, a flushing assembly (39) is arranged on the inner wall of an upper flushing chamber (61), and the flushing assembly (39) is connected with the transverse sliding column (36);
the baffle assembly (35) includes: baffle (71) that can cover export (34) in the top, arc slide (72) set up in baffle (71) are close to sideslip traveller (36) end, driving roller (37) sliding connection in on arc slide (72), spacing sliding sleeve (73) install in baffle (71) length direction's both ends, spacing horizontal pole (74) fixed mounting in top in lower aeration zone (31), spacing sliding sleeve (73) cover is located on spacing horizontal pole (74), reset spring (75) cover is located on spacing horizontal pole (74) to support and locate on spacing sliding sleeve (73).
2. The total nitrogen removal device for sewage according to claim 1, wherein the anaerobic zone (2) is arranged in a bucket shape, and the water outlet end of the flushing water delivery assembly (6) is abutted against the inner wall of the anaerobic zone (2) and extends to the bottom position in the anaerobic zone (2).
3. The total nitrogen removal device for sewage according to claim 1, wherein a stirrer (21) and anaerobic activated sludge are arranged in the anaerobic zone (2).
4. A total nitrogen sewage removal unit according to claim 1, wherein the overflow assembly (5) comprises: the circumference is seted up in overflow launder (51) that upper sedimentation zone (32) inner wall is close to top position, overflow tank (52) install in upper sedimentation zone (32) side, and with overflow launder (51) are connected, overflow tank (52) are located wash out in water delivery subassembly (6), U type overflow pipe (53) one end stretch into wash out in water delivery subassembly (6), and with overflow tank (52) are connected, U type overflow pipe (53) other end stretch into in filtration zone (4), U type overflow pipe (53) are close to overflow tank (52) end height be greater than U type overflow pipe (53) are close to filtration zone (4) end height.
5. A total nitrogen removal unit for sewage according to claim 4, wherein said filtering zone (4) comprises: the water outlet device comprises a bottom water outlet region (41), a water outlet (12) and a top filtering region (42) are connected with the bottom water outlet region (41), the top filtering region (42) is located above the bottom water outlet region (41), an MBR filter membrane component is installed in the top filtering region (42), the other end of a U-shaped overflow pipe (53) stretches into the top filtering region (42) and is located above the MBR filter membrane component, a water filtering cap (43) is installed at the bottom in the top filtering region (42) and is connected with the bottom water outlet region (41), one end of a back flushing pipe (44) penetrates through a shell (10) and stretches into the top filtering region (42) from the top end of the top filtering region (42), a back flushing valve (45) is installed at the other end of the back flushing pipe (44), and a window is installed on the surface of the shell (10) and is connected with the top filtering region (42).
6. A total nitrogen removal apparatus for sewage according to claim 4, wherein said flushing water supply assembly (6) comprises: the upper flushing chamber (61) is arranged above the filtering area (4), the water inlet (11) is connected with the upper flushing chamber (61), the bottom in the upper flushing chamber (61) is arranged in a lower inclined mode, one end of the lower flushing pipe (62) is connected with the bottom end of the upper flushing chamber (61), and the other end of the lower flushing pipe (62) is attached to the inner wall of the anaerobic area (2) and extends to the bottom position in the anaerobic area (2).
7. A total nitrogen removal apparatus for wastewater as claimed in claim 4 wherein said flushing assembly (39) comprises: the automatic flushing device comprises a supporting seat (70) fixedly arranged on the inner wall of an upper flushing chamber (61), a turnover rod (76) is arranged in an obtuse angle bending mode, the turnover rod (76) is hinged to the bottom end of the supporting seat (70) through a mounting shaft, a reset torsion spring is sleeved on the mounting shaft, a transmission sliding chute (77) is arranged on the turnover rod (76), one end of a transmission cross rod (78) stretches into the lower aeration zone (31) and is connected with a transverse sliding column (36), the other end of the transmission cross rod (78) stretches into the upper flushing chamber (61), a limit sliding block (79) is slidably connected in the transmission sliding chute (77), the limit sliding block (79) is connected with the other end of the transmission cross rod (78), and a flushing plate (63) is arranged on the turnover rod (76).
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| Application Number | Priority Date | Filing Date | Title |
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| CN202310051249.4A CN116022966B (en) | 2023-02-02 | 2023-02-02 | Sewage total nitrogen removing device |
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| CN202310051249.4A CN116022966B (en) | 2023-02-02 | 2023-02-02 | Sewage total nitrogen removing device |
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Citations (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN200940108Y (en) * | 2006-08-15 | 2007-08-29 | 武汉加华科技有限公司 | Integrated, up-flow type aeration and filtration wastewater treatment equipment |
| CN101357814A (en) * | 2008-09-02 | 2009-02-04 | 深圳清华大学研究院 | Linkage processing method and apparatus of circulatory flow multiplex biochemistry and filtrating |
| CN207435149U (en) * | 2017-11-10 | 2018-06-01 | 江苏聚仁环境工程有限公司 | A kind of integration MBR sewage disposal devices |
| CN208532540U (en) * | 2018-05-29 | 2019-02-22 | 四川玖清环保设备有限公司 | Integrated sewage treating apparatus |
| CN112759080A (en) * | 2020-12-30 | 2021-05-07 | 武汉飞博乐环保工程有限公司 | Rapid biochemical treatment facility and treatment method for sewage |
| CN114735903A (en) * | 2022-06-13 | 2022-07-12 | 金科环境股份有限公司 | Sewage total nitrogen removal device and operation method thereof |
| CN115321682A (en) * | 2022-07-22 | 2022-11-11 | 北京化工大学 | Upflow type continuous aerobic granular sludge reaction device and process |
| CN218146054U (en) * | 2022-07-29 | 2022-12-27 | 清华苏州环境创新研究院 | Sewage treatment purifies groove |
Family Cites Families (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US8163174B2 (en) * | 2010-01-28 | 2012-04-24 | Jun-Nan Lin | Submerged biofiltration purifying apparatus |
| CN109879425B (en) * | 2019-03-29 | 2022-11-25 | 云南合续环境科技股份有限公司 | Equipment for advanced phosphorus and nitrogen removal of sewage treatment |
-
2023
- 2023-02-02 CN CN202310051249.4A patent/CN116022966B/en active Active
Patent Citations (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN200940108Y (en) * | 2006-08-15 | 2007-08-29 | 武汉加华科技有限公司 | Integrated, up-flow type aeration and filtration wastewater treatment equipment |
| CN101357814A (en) * | 2008-09-02 | 2009-02-04 | 深圳清华大学研究院 | Linkage processing method and apparatus of circulatory flow multiplex biochemistry and filtrating |
| CN207435149U (en) * | 2017-11-10 | 2018-06-01 | 江苏聚仁环境工程有限公司 | A kind of integration MBR sewage disposal devices |
| CN208532540U (en) * | 2018-05-29 | 2019-02-22 | 四川玖清环保设备有限公司 | Integrated sewage treating apparatus |
| CN112759080A (en) * | 2020-12-30 | 2021-05-07 | 武汉飞博乐环保工程有限公司 | Rapid biochemical treatment facility and treatment method for sewage |
| CN114735903A (en) * | 2022-06-13 | 2022-07-12 | 金科环境股份有限公司 | Sewage total nitrogen removal device and operation method thereof |
| CN115321682A (en) * | 2022-07-22 | 2022-11-11 | 北京化工大学 | Upflow type continuous aerobic granular sludge reaction device and process |
| CN218146054U (en) * | 2022-07-29 | 2022-12-27 | 清华苏州环境创新研究院 | Sewage treatment purifies groove |
Non-Patent Citations (1)
| Title |
|---|
| 厌氧/一体化工艺处理生活污水运行特性研究;侯琳;陈敏东;李德豪;周如金;林红艺;;环境科学与技术(第09期);第113-116页 * |
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Effective date of registration: 20240419 Address after: 224000 West of Zhansheng Road and South of Hongye Road in Hede Town Industrial Park, Sheyang County, Yancheng City, Jiangsu Province Patentee after: Jiangsu Xinnongyuan Water Treatment Equipment Co.,Ltd. Country or region after: China Address before: 224000 No. 1 Hope Avenue Middle Road, Tinghu District, Yancheng City, Jiangsu Province Patentee before: YANCHENG INSTITUTE OF TECHNOLOGY Country or region before: China |