CN109574332A - A kind of organic wastewater rotational flow settlement purifying processing device - Google Patents
A kind of organic wastewater rotational flow settlement purifying processing device Download PDFInfo
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- CN109574332A CN109574332A CN201811267438.0A CN201811267438A CN109574332A CN 109574332 A CN109574332 A CN 109574332A CN 201811267438 A CN201811267438 A CN 201811267438A CN 109574332 A CN109574332 A CN 109574332A
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- 239000002351 wastewater Substances 0.000 title claims abstract description 82
- 238000004062 sedimentation Methods 0.000 claims abstract description 65
- 238000003860 storage Methods 0.000 claims abstract description 33
- 230000001699 photocatalysis Effects 0.000 claims abstract description 9
- 238000000605 extraction Methods 0.000 claims abstract description 7
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 32
- 238000009987 spinning Methods 0.000 claims description 22
- 239000004744 fabric Substances 0.000 claims description 9
- 230000004087 circulation Effects 0.000 claims description 7
- 238000005086 pumping Methods 0.000 claims description 2
- 230000000694 effects Effects 0.000 abstract description 20
- 238000010907 mechanical stirring Methods 0.000 abstract description 7
- 239000002245 particle Substances 0.000 abstract description 5
- 238000004220 aggregation Methods 0.000 abstract description 4
- 230000002776 aggregation Effects 0.000 abstract description 4
- 230000007613 environmental effect Effects 0.000 abstract description 3
- 239000002244 precipitate Substances 0.000 abstract description 3
- 238000004134 energy conservation Methods 0.000 abstract description 2
- 239000013049 sediment Substances 0.000 description 16
- 239000005416 organic matter Substances 0.000 description 15
- 239000000126 substance Substances 0.000 description 11
- 238000000034 method Methods 0.000 description 8
- 238000010586 diagram Methods 0.000 description 6
- 230000008569 process Effects 0.000 description 6
- 239000010802 sludge Substances 0.000 description 5
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 4
- 230000009471 action Effects 0.000 description 3
- 230000003647 oxidation Effects 0.000 description 3
- 238000007254 oxidation reaction Methods 0.000 description 3
- 150000003839 salts Chemical class 0.000 description 3
- CDBYLPFSWZWCQE-UHFFFAOYSA-L Sodium Carbonate Chemical compound [Na+].[Na+].[O-]C([O-])=O CDBYLPFSWZWCQE-UHFFFAOYSA-L 0.000 description 2
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 2
- 230000004888 barrier function Effects 0.000 description 2
- 239000001569 carbon dioxide Substances 0.000 description 2
- 229910002092 carbon dioxide Inorganic materials 0.000 description 2
- 239000003054 catalyst Substances 0.000 description 2
- 239000000701 coagulant Substances 0.000 description 2
- 238000005056 compaction Methods 0.000 description 2
- 238000012851 eutrophication Methods 0.000 description 2
- 230000005484 gravity Effects 0.000 description 2
- 239000012535 impurity Substances 0.000 description 2
- 238000012423 maintenance Methods 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- VUZPPFZMUPKLLV-UHFFFAOYSA-N methane;hydrate Chemical compound C.O VUZPPFZMUPKLLV-UHFFFAOYSA-N 0.000 description 2
- 244000005700 microbiome Species 0.000 description 2
- 239000010815 organic waste Substances 0.000 description 2
- 238000001556 precipitation Methods 0.000 description 2
- 238000003672 processing method Methods 0.000 description 2
- 238000003756 stirring Methods 0.000 description 2
- 238000004065 wastewater treatment Methods 0.000 description 2
- GRYLNZFGIOXLOG-UHFFFAOYSA-N Nitric acid Chemical compound O[N+]([O-])=O GRYLNZFGIOXLOG-UHFFFAOYSA-N 0.000 description 1
- CBENFWSGALASAD-UHFFFAOYSA-N Ozone Chemical compound [O-][O+]=O CBENFWSGALASAD-UHFFFAOYSA-N 0.000 description 1
- ISWSIDIOOBJBQZ-UHFFFAOYSA-N Phenol Chemical compound OC1=CC=CC=C1 ISWSIDIOOBJBQZ-UHFFFAOYSA-N 0.000 description 1
- 238000005273 aeration Methods 0.000 description 1
- 239000003513 alkali Substances 0.000 description 1
- 230000003139 buffering effect Effects 0.000 description 1
- 230000003197 catalytic effect Effects 0.000 description 1
- 238000006555 catalytic reaction Methods 0.000 description 1
- 239000011248 coating agent Substances 0.000 description 1
- 238000000576 coating method Methods 0.000 description 1
- 238000009833 condensation Methods 0.000 description 1
- 230000005494 condensation Effects 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 239000000498 cooling water Substances 0.000 description 1
- 238000009826 distribution Methods 0.000 description 1
- 239000000975 dye Substances 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000005111 flow chemistry technique Methods 0.000 description 1
- 238000011010 flushing procedure Methods 0.000 description 1
- 239000008187 granular material Substances 0.000 description 1
- 230000036541 health Effects 0.000 description 1
- 239000004615 ingredient Substances 0.000 description 1
- 230000001788 irregular Effects 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 229910017604 nitric acid Inorganic materials 0.000 description 1
- 239000000618 nitrogen fertilizer Substances 0.000 description 1
- 231100000252 nontoxic Toxicity 0.000 description 1
- 230000003000 nontoxic effect Effects 0.000 description 1
- 239000013618 particulate matter Substances 0.000 description 1
- 239000000575 pesticide Substances 0.000 description 1
- 239000002686 phosphate fertilizer Substances 0.000 description 1
- 230000000704 physical effect Effects 0.000 description 1
- 231100000614 poison Toxicity 0.000 description 1
- 230000007096 poisonous effect Effects 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 239000010865 sewage Substances 0.000 description 1
- 229910000029 sodium carbonate Inorganic materials 0.000 description 1
- 235000017550 sodium carbonate Nutrition 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 229920002994 synthetic fiber Polymers 0.000 description 1
- 238000005406 washing Methods 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/30—Treatment of water, waste water, or sewage by irradiation
- C02F1/32—Treatment of water, waste water, or sewage by irradiation with ultraviolet light
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/72—Treatment of water, waste water, or sewage by oxidation
- C02F1/725—Treatment of water, waste water, or sewage by oxidation by catalytic oxidation
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F2001/007—Processes including a sedimentation step
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2101/00—Nature of the contaminant
- C02F2101/30—Organic compounds
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- Chemical & Material Sciences (AREA)
- Life Sciences & Earth Sciences (AREA)
- Hydrology & Water Resources (AREA)
- Engineering & Computer Science (AREA)
- Environmental & Geological Engineering (AREA)
- Water Supply & Treatment (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Health & Medical Sciences (AREA)
- Toxicology (AREA)
- Physical Water Treatments (AREA)
Abstract
The invention discloses a kind of organic wastewater rotational flow settlement purifying processing devices, including settlement treatment pond, settlement treatment pond includes the upper storage reservoir room being connected, the room Xia Chi, it is equipped between central vertical pipe central vertical pipe and the locular wall of upper storage reservoir room at the indoor center of upper storage reservoir room and is equipped with connecting plate, the lower section of connecting plate is equipped with ultraviolet lamp tube, the lower section of ultraviolet lamp tube is equipped with photocatalytic plate, outlet pipe is opened up on the locular wall of upper storage reservoir room, central vertical pipe inner wall is equipped with eddy flow component, eddy flow component includes forward spin flow ring, lower cyclone ring, the lower end connection sedimentation plate of central vertical pipe, several through-holes are opened up on sedimentation plate, the extraction mud pipe of connection slush pump is equipped in the room Xia Chi.In the present invention, it is not necessarily to mechanical stirring, reduces the mechanical stirring component of settling tank, energy saving, energy conservation and environmental protection；It precipitates particle and is easy aggregation, be easy sedimentation, effect of settling of the invention is good, and sinking speed is fast；Building cost reduces, and factory is suitble to promote the use of.
Description
Technical field
The present invention relates to chemical wastewater treatment devices, and in particular to a kind of organic wastewater rotational flow settlement purifying processing device.
Background technique
Pure water is changing original physical property or chemical property after using, and becomes containing variety classes
The waste water of impurity.Wastewater from chemical industry be exactly the technique waste water given off in Chemical Manufacture, cooling water, discarded washing water, equipment and
The waste water such as place flushing water.If these waste water are discharged without processing, will cause water body heterogeneity and in various degree
Pollution influence the production of industrial or agricultural to endanger the health of the mankind.Chemical industry effluent can be divided into three categories by ingredient: the
One kind is the waste water containing organic matter, mainly from the waste water of the industries such as basic organic, synthetic material, pesticide, dyestuff discharge；
Second class is the waste water containing inorganic matter, such as inorganic salts, nitrogenous fertilizer, phosphate fertilizer, sulfuric acid, nitric acid and the waste water of soda ash industry discharge；The
Three classes are the not only waste water containing organic matter but also containing organic/inorganic substance, such as chlor-alkali, photosensitive material, coating industry.Wherein containing organic
Most important wastewater from chemical industry at present when the waste water of object.
The treatment process of the existing waste water containing organic matter specifically includes that sedimentation, adjusts pH, is redox, aeration, micro-
The treatment process such as biology, wherein the basic process of settlement treatment room wastewater treatment, the sediment in waste water is discharged, and is conducive to more preferable
Processing waste water.Such as Chinese patent, CN201510835357.6 discloses a kind of high saliferous of high temperature that oilfield sewage softening generates
The processing method of organic wastewater, belongs to environmental technology field.Processing method of the invention is by pretreatment unit, coagulant precipitation list
Five member, ozone oxidation unit, filter element, sludge treating block units successively form, can be by high temperature highly salt containing organic waste water
The separation of the substances such as petroleum-type, volatile phenol, COD, qualified discharge after handling high temperature highly salt containing organic waste water.Sludge treating block will
The sludge that coagulant precipitation generates is handled again, prevents discharge of poisonous waste, resource is utilized effectively.
Existing settling tank generally uses vertical-flow settling tank and cross-flow type settling tank, wherein the building of cross-flow type settling tank
It is at low cost, but take up a large area, it usually needs multiple ponds are arranged in series and parallel, the low efficiency of processing, and vertical-flow settling tank
Occupied area it is small, it is general only to need the good processing organic wastewater of pond energy.
Vertical-flow settling tank in the prior art has the following problems when in use: 1, machine waste water is in modern chemical industry waste water
Main waste water source, and in organic wastewater contain a large amount of organic matter, process of the organic matter in sedimentation, microorganism easy to breed,
Water eutrophication is caused, settling tank is smelly；2, the poor processing effect of organic matter, and processing speed is slow；3, the speed settled is slow,
Cause the height of settling tank higher, the building cost of settling tank is high；4, the sediment in organic wastewater is more, and settle amount of substance compared with
Gently, it is difficult to which effective sedimentation, settling tank in the prior art need mechanical stirring, have motor to drive agitating shaft stirring, so that heavy
Object rapid subsidence drops.
Summary of the invention
The technical problem to be solved in the invention: 1, machine waste water is the main waste water source in modern chemical industry waste water, and organic
Contain a large amount of organic matter in waste water, for organic matter in the process of sedimentation, microorganism easy to breed causes water eutrophication, heavy
It is smelly that pond drops；2, the poor processing effect of organic matter, and processing speed is slow；3, settle speed it is slow, cause the height of settling tank compared with
The building cost of height, settling tank is high；4, the sediment in organic wastewater is more, and sediment lighter weight, it is difficult to effective sedimentation,
Settling tank in the prior art needs mechanical stirring, has motor to drive agitating shaft stirring, so that sediment rapid subsidence.
To solve the above problems, not only taking up an area the invention discloses a kind of organic wastewater rotational flow settlement purifying processing device
Area is small, and work efficiency is high, is not necessarily to mechanical stirring, reduces the mechanical stirring component of settling tank, energy saving, energy-saving ring
It protects；It precipitates particle and is easy aggregation, be easy sedimentation, effect of settling of the invention is good, and sinking speed is fast；Building cost reduces, and is suitble to
Factory promotes the use of.
In order to reach the goals above, the invention provides the following technical scheme:
A kind of organic wastewater rotational flow settlement purifying processing device, including settlement treatment pond, the settlement treatment pond includes phase
Lead to the upper storage reservoir room connect, the room Xia Chi, the center of being equipped with is arranged at below ground, the indoor center of the upper storage reservoir room in the room Xia Chi
Vertical tube, the upper extreme point of the central vertical pipe are higher than the upper extreme point of upper storage reservoir room, and the lower extreme point of the central vertical pipe is located in upper storage reservoir room；
Connecting plate is equipped between the central vertical pipe and the locular wall of upper storage reservoir room, the lower section of the connecting plate is equipped with ultraviolet lamp tube, the purple
The lower section of outer fluorescent tube is equipped with photocatalytic plate, opens up outlet pipe on the locular wall of the upper storage reservoir room, the outlet pipe is located at connecting plate
Lower section, and outlet pipe is located at the top of photocatalytic plate；The top of the central vertical pipe is equipped with water inlet pipe, the central vertical pipe inner wall
Equipped with eddy flow component, the eddy flow component includes forward spin flow ring, lower cyclone ring, and the forward spin flow ring includes upper connection ring, lower solid
Determine ring, spinning disk, the upper connection ring is fixedly connected on the locular wall of upper storage reservoir room, is set between the upper connection ring and lower fixed ring
There are several spinning disks, be staggered between spinning disk, and there are waste water circulation passages between adjacent two panels spinning disk, under described
Cyclone ring is consistent with the shape and structure of forward spin flow ring, and lower cyclone ring is symmetrical arranged along the horizontal plane, under the lower cyclone ring includes
Connection ring, upper fixed ring, spinning disk, the lower connection ring are fixedly connected on the locular wall of upper storage reservoir room, the lower connection ring with it is upper
It is equipped with several spinning disks between fixed ring, is staggered between spinning disk, and there are waste water streams between adjacent two panels spinning disk
Circulation passage；The lower end connection sedimentation plate of the central vertical pipe, one end of the sedimentation plate are fixedly connected with the outer edge of central vertical pipe,
The other end of the sedimentation plate is fixedly connected on the pool wall of upper storage reservoir room, and several through-holes, the sedimentation plate are opened up on the sedimentation plate
Lower section be decanting zone, the top of the sedimentation plate is clean water area, and the room Xia Chi is mud collection area, and pumping is equipped in the room Xia Chi
Mud pipe, the extraction mud pipe connect slush pump, and the outside in settlement treatment pond is arranged in the slush pump.
The technical solution that the present invention further limits, the bottom surface of the sedimentation plate are equipped with the folding with sedimentation plate inclination connection
The tilt angle of flowing plate, the baffle plate and sedimentation plate is 15-45 °.The setting of baffle plate, so that waste water is flowed down from central vertical pipe
Afterwards, it is handled through baffle plate baffling, the sediment in waste water is stopped by baffle plate baffling, and the effect of settling of the sediment in waste water is more
It is good.
The technical solution that the present invention further limits, the bottom surface of the sedimentation plate is equipped with to interlink with the through-hole of sedimentation plate
The sedimentation pipe connect.The setting of sedimentation pipe, so that waste water is settled through sedimentation pipe, so that the effect of sedimentation is more preferable, and reasonable utilization
The space of decanting zone, in effective space, the waste water of increase is in the residence time of decanting zone, so that effect of settling is more preferable.
The technical solution that the present invention further limits, the sedimentation pipe and sedimentation plate inclination connect, the sedimentation pipe and heavy
The tilt angle for dropping plate is 15-30 °.Sedimentation pipe is obliquely installed, and the technical solution that the present invention further limits increases waste water
Residence time in inclined tube, so that the sedimentation of waste water more preferably further increases.
The technical solution that the present invention further limits, the diameter of the fixed ring of the forward spin flow ring are connect ring diameter 1/
10-1/20.The diameter of fixed ring is smaller, so that the eddy flow angle of spinning disk is bigger, the effect of centrifugal cyclone is more preferable, in waste water
Sediment is easier to settle.
The technical solution that the present invention further limits, the sedimentation processing device are additionally provided with ladder, and the ladder setting exists
On the pond outer wall in settlement treatment pond.Maintenance is observed in the convenient inside to settling tank of the setting of ladder, while by ladder setting heavy
On the pond outer wall for dropping pond, construction cost is saved.
The technical solution that the present invention further limits, the section of the room Xia Chi are taper, trapezoidal one of which.Will under
The section setting of expansion chamber is tapered or trapezoidal, so that the better effect of the storage settled sludge of the room Xia Chi.
The technical solution that the present invention further limits, there are certain gap between the forward spin flow ring and lower cyclone ring,
Cloth flowing plate is equipped between the forward spin flow ring and lower cyclone ring, the cloth flowing plate is equipped with through-hole.Due to forward spin flow ring and backspin
Being symmetrical arranged for ring is flowed, so that the vortex of the water flow of eddy flow is contrary, water flow is more anxious, and cloth flowing plate plays certain distribution
The effect of buffering.
The working principle of the invention: organic wastewater from top to bottom enters in settling tank out of central vertical pipe, perpendicular at center
In pipe, via swirler assembly eddy flow, waste water forms the water flow of eddy flow, especially in the present invention under the action of gravity and centrifugal force
Eddy flow component includes forward spin flow ring, lower cyclone ring, and waste water is after eddy flow twice, the effect of impurity particle in waste water in centrifugal force
Lower aggregation forms sediment, and then, the sediment in waste water and waste water enters decanting zone, in decanting zone, sediment sedimentation
It drops into the room Xia Chi, is extracted out through slush pump；Then the organic wastewater after settling does not settle through settling baffling, the barrier of plate
Particle sediment further drops into decanting zone by sedimentation plate barrier, and the organic wastewater for settling completion rises into clean water area,
In clean water area, organic wastewater is catalyzed through the photochemical catalyst on photochemical catalyst plate under the irradiation of ultraviolet lamp, having in clean water area
Organic matter is resolved into carbon dioxide and water by the organic matter photochemical catalytic oxidation in machine waste water, realizes good removal organic matter
Effect.Waste water after the completion of processing is discharged from outlet pipe.
Compared with prior art, the invention has the following advantages: 1, in the present invention, waste water enters forward spin flow ring
It is interior, the water flow of eddy flow is formed, subsequently into rear lower cyclone ring, the water flow of the eddy flow of opposite direction is formed, so that in waste water
The uniform whirl condensation of sediment is reunited, and is formed the effect that certain water flow is agglomerated automatically, is functioned as agitating shaft, still
Agitating shaft is using applied force, and eddy flow of the invention is the inertia force of water flow itself, and therefore, the present invention is stirred without machinery
It mixes, reduces the mechanical stirring component of settling tank, energy saving, energy conservation and environmental protection；2, the granule foreign in the present invention, via swirler assembly
Eddy flow processing, waste water form the water flow of vortex, and the particulate matter in waste water precipitates particle under the double action of centrifugal force and gravity
It is easy aggregation, is easy sedimentation, effect of settling of the invention is good, and sinking speed is fast；3, organic wastewater of the invention ultraviolet lamp tube,
Under the action of photocatalytic plate, catalysis oxidation occurs for organic matter, and organic matter resolves into nontoxic carbon dioxide and water, processes
Journey is simple, and is not necessarily to manual operation；The high treating effect of organic matter, and processing speed is fast；4, structure setting of the invention is reasonable,
The setting of eddy flow component increases the sinking speed of waste water, and the height of settling tank reduces, so that the building cost of settling tank drops
It is low, it is suitble to factory to promote the use of.
Detailed description of the invention
Fig. 1 is the structural diagram of the present invention；
Fig. 2 is structural schematic diagram of the invention (band ladder)；
Fig. 3 is the top view of attached drawing 2 of the invention；
Fig. 4 is forward spin flow ring structure schematic diagram of the invention
Fig. 5 is the top view of forward spin flow ring of the invention；
Fig. 6 is the structural schematic diagram of lower cyclone ring of the invention；
Fig. 7 is a schematic structural view of Embodiment 2 of the present invention；
Fig. 8 is the settlement compaction structure schematic diagram of the embodiment of the present invention 2；
Fig. 9 is a schematic structural view of Embodiment 3 of the present invention；
Figure 10 is the settlement compaction structure schematic diagram of the embodiment of the present invention 3；
Reference signs list: 100, settlement treatment pond；200, upper storage reservoir room；300, the room Xia Chi；400, decanting zone；500, water purification
Area；1, central vertical pipe；2, connecting plate；3, ultraviolet lamp tube；4, photocatalytic plate；5, outlet pipe；6, water inlet pipe；7, eddy flow component；71,
Forward spin flow ring；711, upper connection ring；712, lower fixed ring；713, forward spin flow piece；72, lower cyclone ring；721, lower connection ring；722,
Upper fixed ring；723, lower spinning disk；73, circulation passage；8, plate is settled；9, extraction mud pipe；10, slush pump；11, ladder；12, cloth stream
Plate；13, baffle plate；14, sedimentation pipe.
Specific embodiment
Technical solution of the present invention is described in detail below by attached drawing.
Embodiment 1:
As shown in Figure 1, Figure 2, shown in Fig. 3, Fig. 4, Fig. 5, Fig. 6, a kind of organic wastewater rotational flow settlement purifying processing device, including it is heavy
Processing pond 100 drops, while realizing the settlement treatment to organic wastewater by settlement treatment pond, purifying organic.Settlement treatment
Pond includes the upper storage reservoir room 200 being connected, the room Xia Chi 300, and the setting of the room Xia Chi first digs ground, so in below ground on the ground
Settlement treatment pond is built on ground afterwards, the section in settlement treatment pond is circle in embodiment of the invention, certainly, according to reality
Border needs, and can also say the section setting squarely or other irregular shapes in settlement treatment pond.
Central vertical pipe 1 is equipped at the indoor center of upper storage reservoir room, the upper extreme point of central vertical pipe is higher than the upper extreme point of upper storage reservoir room, in
The lower extreme point of heart vertical tube is located in upper storage reservoir room；Connecting plate 2, the lower section of connecting plate are equipped between central vertical pipe and the locular wall of upper storage reservoir room
Equipped with ultraviolet lamp tube 3, the lower section of ultraviolet lamp tube is equipped with photocatalytic plate 4, opens up outlet pipe 5, outlet pipe position on the locular wall of upper storage reservoir room
In the lower section of connecting plate, and outlet pipe is located at the top of photocatalytic plate；The top of central vertical pipe is equipped with water inlet pipe 6, central vertical pipe
Inner wall is equipped with eddy flow component 7, and eddy flow component includes forward spin flow ring 71, lower cyclone ring 72, forward spin flow ring include upper connection ring 711,
Lower fixed ring 712, forward spin flow piece 713, upper connection ring are fixedly connected on the locular wall of upper storage reservoir room, upper connection ring and lower fixed ring it
Between be equipped with several forward spin flow pieces, be staggered between forward spin flow piece, and there are waste water circulations between adjacent two panels forward spin flow piece
Channel 73, lower cyclone ring is consistent with the shape and structure of forward spin flow ring, and lower cyclone ring is symmetrical arranged along the horizontal plane, lower cyclone ring packet
Lower connection ring 721, upper fixed ring 722, lower spinning disk 723 are included, lower connection ring is fixedly connected on the locular wall of upper storage reservoir room, lower connection
Be equipped with several lower spinning disks between ring and upper fixed ring, be staggered between lower spinning disk, and under adjacent two panels spinning disk it
Between there are waste water circulation passages；The lower end connection sedimentation plate 8 of central vertical pipe, the one end for settling plate is fixedly connected with the outer of central vertical pipe
Edge, the other end for settling plate are fixedly connected on the pool wall of upper storage reservoir room, are settled and are opened up several through-holes 81 on plate, settle the lower section of plate
For decanting zone 400, the top for settling plate is clean water area 500, and the room Xia Chi is mud collection area, is equipped with extraction mud pipe 9, extraction mud pipe in the room Xia Chi
Slush pump 10 is connected, the outside in settlement treatment pond is arranged in slush pump.
The diameter of the fixed ring of forward spin flow ring is the 1/10-1/20 for connecting ring diameter, in the present embodiment, specially upper rotation
The diameter for flowing the fixed ring of ring is connect ring diameter 1/15.The diameter of fixed ring is smaller, so that the eddy flow angle of spinning disk is more
Greatly, the effect of centrifugal cyclone is more preferable, and the sediment in waste water is easier to settle.
In the present embodiment, sedimentation processing device is additionally provided with ladder 11, and ladder is arranged on the pond outer wall in settlement treatment pond.
Maintenance is observed in the convenient inside to settling tank of the setting of ladder, while ladder being arranged on the pond outer wall of settling tank, and saving is built
Cause this.
In the present embodiment, the section of the room Xia Chi is taper, trapezoidal one of which.The section of bottom setting chamber is arranged to
Taper is trapezoidal, so that the better effect of the storage settled sludge of the room Xia Chi.
In the present embodiment, there are certain gap, forward spin flow ring and lower cyclone rings between forward spin flow ring and lower cyclone ring
Between be equipped with cloth flowing plate 12, cloth flowing plate be equipped with through-hole.Due to being symmetrical arranged for forward spin flow ring and lower cyclone ring, so that eddy flow
The vortex of water flow it is contrary, water flow is more anxious, and cloth flowing plate plays the role of certain distributed buffer.
In the present embodiment, sedimentation plate vertical with central vertical pipe can be connect, and sedimentation plate can also be tilted with central vertical pipe and be connected.
Embodiment 2
As shown in Figure 7, Figure 8, in the present embodiment, the bottom surface for settling plate is equipped with the baffle plate connected with sedimentation plate inclination
13, baffle plate and the tilt angle for settling plate are 15-45 °.The setting of baffle plate, so that after waste water is flowed down from central vertical pipe, warp
Baffle plate baffling is handled, and the sediment in waste water is stopped by baffle plate baffling, and the effect of settling of the sediment in waste water is more preferable.
Remaining structure is same as Example 1, and details are not described herein.
Embodiment 3
As shown in Figure 9, Figure 10, in the present embodiment, the bottom surface for settling plate is equipped with to be connected with the through-hole of sedimentation plate
Sedimentation pipe 14.The setting of sedimentation pipe, so that waste water is settled through sedimentation pipe, so that the effect of sedimentation is more preferable, and reasonable utilization
The space of decanting zone, in effective space, the waste water of increase is in the residence time of decanting zone, so that effect of settling is more preferable.
In the present embodiment, sedimentation pipe and sedimentation plate inclination connect, and the tilt angle of the sedimentation pipe and sedimentation plate is 15-
30°.Sedimentation pipe is obliquely installed, and further increases residence time of the waste water in inclined tube, so that the sedimentation of waste water is more preferable
It further increases.
Remaining structure is same as Example 1, and details are not described herein.
As above, it although the present invention has been indicated and described referring to specific preferred embodiment, shall not be construed as pair
The limitation of invention itself.Without prejudice to the spirit and scope of the invention as defined in the appended claims, can to its
It makes a variety of changes in form and in details.
Claims (8)
1. a kind of organic wastewater rotational flow settlement purifying processing device, it is characterised in that: described heavy including settlement treatment pond (100)
Drop processing pond (100) includes the upper storage reservoir room (200) being connected, the room Xia Chi (300), and the room Xia Chi (300) is arranged on ground
Hereinafter, being equipped with central vertical pipe (1) at the indoor center of the upper storage reservoir room (200), the upper extreme point of the central vertical pipe (1) is higher than upper
The upper extreme point of pond room (200), the lower extreme point of the central vertical pipe (1) are located in upper storage reservoir room (200)；The central vertical pipe (1) with
Connecting plate (2) are equipped between the locular wall of upper storage reservoir room (200), the lower section of the connecting plate (2) is equipped with ultraviolet lamp tube (3), the purple
The lower section of outer fluorescent tube (3) is equipped with photocatalytic plate (4), opens up outlet pipe (5), the water outlet on the locular wall of the upper storage reservoir room (200)
Pipe (5) is located at the lower section of connecting plate (2), and outlet pipe (5) is located at the top of photocatalytic plate (4)；The central vertical pipe (1) it is upper
Side is equipped with water inlet pipe (6), and central vertical pipe (1) inner wall is equipped with eddy flow component (7), and the eddy flow component (7) includes forward spin flow
Ring (71), lower cyclone ring (72), the forward spin flow ring (71) include upper connection ring (711), lower fixed ring (712), spinning disk, institute
It states connection ring (711) to be fixedly connected on the locular wall of upper storage reservoir room (200), the upper connection ring (711) and lower fixed ring (712)
Between be equipped with several spinning disks, be staggered between spinning disk, and there are waste water circulation passages between adjacent two panels spinning disk
(73), the lower cyclone ring (72) is consistent with the shape and structure of forward spin flow ring (71), and lower cyclone ring (72) is symmetrical along the horizontal plane
Setting, the lower cyclone ring (72) includes lower connection ring (721), upper fixed ring (722), spinning disk, the lower connection ring (721)
It is fixedly connected on the locular wall of upper storage reservoir room (200), several rotations is equipped between the lower connection ring (721) and upper fixed ring (722)
Flow is staggered between spinning disk, and there are waste water circulation passage (73) between adjacent two panels spinning disk；The center is perpendicular
Lower end connection sedimentation plate (8) of (1) is managed, one end of sedimentation plate (8) is fixedly connected with the outer edge of central vertical pipe (1), described
The other end of sedimentation plate (8) is fixedly connected on the pool wall of upper storage reservoir room (200), opens up several through-holes on the sedimentation plate (8), described
The lower section for settling plate (8) is decanting zone (400), and the top of sedimentation plate (8) is clean water area (500), the room Xia Chi (300)
For mud collection area, the room Xia Chi (300) is interior to be equipped with extraction mud pipe (9), and the extraction mud pipe (9) connects slush pump (10), the pumping mud
(10) setting is pumped in the outside of settlement treatment pond (100).
2. organic wastewater rotational flow settlement purifying processing device according to claim 1, it is characterised in that: the sedimentation plate
(8) bottom surface is equipped with the baffle plate (13) with sedimentation plate (8) inclination connection, and the baffle plate (13) is inclined with sedimentation plate (8)
Rake angle is 15-45 °.
3. organic wastewater rotational flow settlement purifying processing device according to claim 1, it is characterised in that: the sedimentation plate
(8) bottom surface is equipped with the sedimentation pipe (14) being connected with the through-hole of sedimentation plate (8).
4. organic wastewater rotational flow settlement purifying processing device according to claim 3, it is characterised in that: the sedimentation pipe
(14) it is connected with sedimentation plate (8) inclination, the tilt angle of the sedimentation pipe (14) and sedimentation plate (8) is 15-30 °.
5. organic wastewater rotational flow settlement purifying processing device according to claim 1, it is characterised in that: the forward spin flow ring
(71) diameter of fixed ring is the 1/10-1/20 for connecting ring diameter.
6. organic wastewater rotational flow settlement purifying processing device according to claim 1, it is characterised in that: the settlement treatment
Device is additionally provided with ladder (11), and the ladder (11) is arranged on the pond outer wall of settlement treatment pond (100).
7. organic wastewater rotational flow settlement purifying processing device according to claim 1, it is characterised in that: the room Xia Chi
(300) section is taper, trapezoidal one of which.
8. organic wastewater rotational flow settlement purifying processing device according to claim 1, it is characterised in that: the forward spin flow ring
(71) there are certain gaps between lower cyclone ring (72), and cloth is equipped between the forward spin flow ring (71) and lower cyclone ring (72)
Flowing plate (12), the cloth flowing plate (12) are equipped with through-hole.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201811267438.0A CN109574332A (en) | 2018-10-29 | 2018-10-29 | A kind of organic wastewater rotational flow settlement purifying processing device |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201811267438.0A CN109574332A (en) | 2018-10-29 | 2018-10-29 | A kind of organic wastewater rotational flow settlement purifying processing device |
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| Publication Number | Publication Date |
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| CN109574332A true CN109574332A (en) | 2019-04-05 |
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ID=65920737
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| CN201811267438.0A Pending CN109574332A (en) | 2018-10-29 | 2018-10-29 | A kind of organic wastewater rotational flow settlement purifying processing device |
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| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US6063279A (en) * | 1997-09-18 | 2000-05-16 | Sharp Kabushiki Kaisha | Waste water treatment method and equipment being able to treat hydrogen peroxide, phosphorus, fluorine and organic-matters with high efficiency |
| EP1470858A1 (en) * | 2003-04-25 | 2004-10-27 | Tommy Chi-Kin Wong | Device for treating by photocatalysis a swirling fluid |
| CN1951828A (en) * | 2006-09-25 | 2007-04-25 | 同济大学 | Energy-saving highly-efficient photocatalysis and film filter water treatment system |
| CN103382066A (en) * | 2013-07-18 | 2013-11-06 | 李榕生 | Photocatalysis waste water degradation reactor for self state inspection of electrodeless ultraviolet lamp |
| CN206660759U (en) * | 2017-03-24 | 2017-11-24 | 上海江柘环境工程技术有限公司 | Vertical sedimentation basin |
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