CN107500398A - A kind of nanoparticle rotational flow aeration device - Google Patents
A kind of nanoparticle rotational flow aeration device Download PDFInfo
- Publication number
- CN107500398A CN107500398A CN201710907106.3A CN201710907106A CN107500398A CN 107500398 A CN107500398 A CN 107500398A CN 201710907106 A CN201710907106 A CN 201710907106A CN 107500398 A CN107500398 A CN 107500398A
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- CN
- China
- Prior art keywords
- nanoparticle
- main body
- aeration device
- rotational flow
- cyclone main
- Prior art date
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- 239000002105 nanoparticle Substances 0.000 title claims abstract description 76
- 238000005273 aeration Methods 0.000 title claims abstract description 32
- CBENFWSGALASAD-UHFFFAOYSA-N Ozone Chemical compound [O-][O+]=O CBENFWSGALASAD-UHFFFAOYSA-N 0.000 claims abstract description 30
- 239000000463 material Substances 0.000 claims abstract description 30
- 239000008188 pellet Substances 0.000 claims abstract description 28
- -1 hydroxyl radical free radical Chemical class 0.000 claims abstract description 13
- 150000002500 ions Chemical class 0.000 claims abstract description 12
- 230000004913 activation Effects 0.000 claims abstract description 11
- 238000009825 accumulation Methods 0.000 claims abstract description 8
- 210000002985 organ of corti Anatomy 0.000 claims abstract description 7
- 238000011144 upstream manufacturing Methods 0.000 claims abstract description 6
- 239000001301 oxygen Substances 0.000 claims description 17
- 229910052760 oxygen Inorganic materials 0.000 claims description 17
- 239000003054 catalyst Substances 0.000 claims description 13
- 239000007787 solid Substances 0.000 claims description 12
- 239000000843 powder Substances 0.000 claims description 8
- 229920000122 acrylonitrile butadiene styrene Polymers 0.000 claims description 6
- 230000001186 cumulative effect Effects 0.000 claims description 4
- 239000007789 gas Substances 0.000 claims description 4
- 239000002245 particle Substances 0.000 claims description 4
- 230000008859 change Effects 0.000 claims description 2
- 239000002351 wastewater Substances 0.000 abstract description 14
- 150000001450 anions Chemical class 0.000 abstract description 4
- 230000003197 catalytic effect Effects 0.000 abstract description 4
- 238000000746 purification Methods 0.000 abstract description 4
- 230000008901 benefit Effects 0.000 abstract description 2
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 15
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 13
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 8
- 239000000499 gel Substances 0.000 description 7
- 238000005276 aerator Methods 0.000 description 6
- 230000000694 effects Effects 0.000 description 6
- QPLDLSVMHZLSFG-UHFFFAOYSA-N Copper oxide Chemical compound [Cu]=O QPLDLSVMHZLSFG-UHFFFAOYSA-N 0.000 description 4
- XLOMVQKBTHCTTD-UHFFFAOYSA-N Zinc monoxide Chemical compound [Zn]=O XLOMVQKBTHCTTD-UHFFFAOYSA-N 0.000 description 4
- 229910044991 metal oxide Inorganic materials 0.000 description 4
- 150000004706 metal oxides Chemical class 0.000 description 4
- 238000012545 processing Methods 0.000 description 4
- 229910052761 rare earth metal Inorganic materials 0.000 description 3
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 2
- 241000700605 Viruses Species 0.000 description 2
- 230000001070 adhesive effect Effects 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 2
- 229960004643 cupric oxide Drugs 0.000 description 2
- 238000000354 decomposition reaction Methods 0.000 description 2
- 230000007613 environmental effect Effects 0.000 description 2
- 239000003292 glue Substances 0.000 description 2
- 230000006872 improvement Effects 0.000 description 2
- 239000007788 liquid Substances 0.000 description 2
- 229910052751 metal Inorganic materials 0.000 description 2
- 239000002184 metal Substances 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 230000003647 oxidation Effects 0.000 description 2
- 238000007254 oxidation reaction Methods 0.000 description 2
- TWNQGVIAIRXVLR-UHFFFAOYSA-N oxo(oxoalumanyloxy)alumane Chemical compound O=[Al]O[Al]=O TWNQGVIAIRXVLR-UHFFFAOYSA-N 0.000 description 2
- 239000010865 sewage Substances 0.000 description 2
- 238000001179 sorption measurement Methods 0.000 description 2
- 229910052613 tourmaline Inorganic materials 0.000 description 2
- 229940070527 tourmaline Drugs 0.000 description 2
- 239000011032 tourmaline Substances 0.000 description 2
- 238000003911 water pollution Methods 0.000 description 2
- 239000011787 zinc oxide Substances 0.000 description 2
- 241001465754 Metazoa Species 0.000 description 1
- XUIMIQQOPSSXEZ-UHFFFAOYSA-N Silicon Chemical compound [Si] XUIMIQQOPSSXEZ-UHFFFAOYSA-N 0.000 description 1
- 230000009471 action Effects 0.000 description 1
- XKMRRTOUMJRJIA-UHFFFAOYSA-N ammonia nh3 Chemical compound N.N XKMRRTOUMJRJIA-UHFFFAOYSA-N 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- 239000008246 gaseous mixture Substances 0.000 description 1
- 239000004519 grease Substances 0.000 description 1
- 229910001385 heavy metal Inorganic materials 0.000 description 1
- 239000000017 hydrogel Substances 0.000 description 1
- 125000002887 hydroxy group Chemical group [H]O* 0.000 description 1
- 229910052500 inorganic mineral Inorganic materials 0.000 description 1
- 229910052747 lanthanoid Inorganic materials 0.000 description 1
- 150000002602 lanthanoids Chemical class 0.000 description 1
- 238000003801 milling Methods 0.000 description 1
- 239000011707 mineral Substances 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000035772 mutation Effects 0.000 description 1
- 239000005416 organic matter Substances 0.000 description 1
- 238000012856 packing Methods 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 230000008569 process Effects 0.000 description 1
- 150000003254 radicals Chemical class 0.000 description 1
- 150000002910 rare earth metals Chemical class 0.000 description 1
- 229910052710 silicon Inorganic materials 0.000 description 1
- 239000010703 silicon Substances 0.000 description 1
- 239000000377 silicon dioxide Substances 0.000 description 1
- 238000005728 strengthening Methods 0.000 description 1
- 238000006467 substitution reaction Methods 0.000 description 1
- 239000000725 suspension Substances 0.000 description 1
- 238000003786 synthesis reaction Methods 0.000 description 1
- 238000004065 wastewater treatment Methods 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
- C02F1/72—Treatment of water, waste water, or sewage by oxidation
- C02F1/78—Treatment of water, waste water, or sewage by oxidation with ozone
-
- 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
Abstract
The present invention relates to a kind of nanoparticle rotational flow aeration device, it includes cyclone main body, cruciform joint and nanoparticle box, the open top of cyclone main body, through hole is offered in the middle part of the bottom wall of cyclone main body, cutting thorn and spiral organ are provided with cyclone main body, nanoparticle box has hollow cavity and its top is provided with the outlet pipe connected with hollow cavity, accumulation has capable of releasing negative ion and catalytic activation ozone pellet nanoparticle material in hollow cavity, the bottom wall and/or side wall of nanoparticle box offer multiple inlet openings, cruciform joint is intersected by vertical tube and transverse tube to be formed, the upper end of vertical tube is connected with through hole, the lower end of vertical tube and the upper end of outlet pipe connect, the both ends of transverse tube are respectively air inlet mouth of pipe and outlet mouth of pipe, air inlet mouth of pipe is connected by upstream inlet pipe with air blower.Advantage is that nanoparticle rotational flow aeration device provided by the invention can effectively improve the content of ozone, anion and hydroxyl radical free radical in waste water, so as to greatly strengthen wastewater purification efficiency.
Description
Technical field
The present invention relates to a kind of water treatment aeration device, and in particular to a kind of nanoparticle rotational flow aeration device.
Background technology
Now, the speed of waste water control is unable to catch up with the speed of water source water pollution, and artificial water of administering is unable to catch up with water pollution speed,
It is unable to catch up with the speed of mutation of virus to virus understanding, the speed of organic synthesis is unable to catch up with the degraded of organic matter, and earth ecology is extensive
Multiple is unable to catch up with what modern Economy Development destroyed.Sanitary wastewater fat content is high, and suspension is high, and cod is high, and ammonia nitrogen is high, heavy metal
Height, people around and animals and plants living environment are seriously affected.If can not be to being fitted as the sanitary wastewater in pollution source
Work as processing, then after it enters water circulation system, administer the very fast increase of more difficult and treatment cost.
At present, a kind of effective ways of sanitary wastewater processing are to be continually fed into by aerator into it with Strong oxdiative
Ozone (the O of effect3), negative oxygen ion (O2 -) with the mixed gas of air, can be good at aoxidizing with the grease ensured in waste water
Degraded.Ozone is generally produced by ozone generator, and negative oxygen ion generally bears the generation of oxygen maker by high-pressure electrostatic.Aerator is to expose
Common aerator in gas pond, also referred to as gas-liquid flow mixing device, aerator is passed through by air, is that the aeration medium in aeration tank carries
Oxygen and the effect of gas-liquid mixed flow, make aeration medium efficiently mix, especially improve the dissolved oxygen content of medium.It is currently used
A kind of method being oxygenated in high sewage is to produce pressure air by air blower, and oxygen is delivered into sewage by aerator, wherein
Rotational flow aeration device is stronger for the ability for increasing oxygen in water.By air blower by the gaseous mixture of ozone, negative oxygen ion and air
Body is passed through rotational flow aeration device and to when being persistently aerated into waste water from it, and the loss of ozone and negative oxygen ion is larger, and many is smelly
Oxygen Auto-decomposition is oxygen (decomposition invalid to wastewater treatment) or to be overflowed from water, the ozone that can be efficiently entering in waste water and
Negative oxygen ion is limited, and then have impact on final wastewater purification effect.
The content of the invention
The present invention provides a kind of nanoparticle rotational flow aeration device, it is desirable to provide one kind can be effectively increased ozone in water and negative oxygen
The rotational flow aeration device of ion concentration, to improve wastewater purification effect.
The technical scheme that the present invention solves above-mentioned technical problem is as follows：A kind of nanoparticle rotational flow aeration device, it includes rotation
It is to be vertically arranged barrel-shaped, the top of the cyclone main body to flow main body, cruciform joint and nanoparticle box, the cyclone main body
Opening, the bottom wall middle part of the cyclone main body offer through hole, cutting thorn and spiral organ, the spiral shell are provided with the cyclone main body
Spigot is arranged at the lower section of the cutting thorn, and the nanoparticle box has hollow cavity and its top is provided with and the middle cavity
The outlet pipe of body connection, the interior accumulation of the hollow cavity have capable of releasing negative ion and catalytic activation ozone pellet nanoparticle material
Material, the bottom wall and/or side wall of the nanoparticle box offer multiple inlet openings, and the cruciform joint is by a vertical tube and one
Transverse tube is crossed as cross and interconnected to form, and the upper end of the vertical tube is connected with the through hole, the lower end of the vertical tube and institute
The upper end connection of outlet pipe is stated, the both ends of the transverse tube are respectively air inlet mouth of pipe and outlet mouth of pipe, and the air inlet mouth of pipe passes through upper
Trip air inlet pipe connects with air blower, and the upstream inlet pipe also connects with ozone generating-device and negative oxygen ion generating means respectively
Logical, the outlet mouth of pipe is closed by sealing-plug or by downstream inlet pipe and another nanoparticle rotational flow aeration device
The air inlet mouth of pipe connection.
On the basis of above-mentioned technical proposal, the present invention can also do following improvement.
Further, the cutting is pierced as multiple bodies of rod that uniform intervals are set in the cyclone main body inwall circumference, institute
Radial direction stretching, extension of the body of rod along the cyclone main body is stated, one end of the body of rod and the inwall of the cyclone main body fix company
Connect, the other end is close to the central axis of the cyclone main body, and each uniform intervals are provided with cutting sheet, Mei Gesuo on the body of rod
Cutting sheet is stated vertically to set.
Further, the lower end of the vertical tube is provided with external screw thread, and the upper end of the outlet pipe is provided with and the external screw thread phase
The internal thread matched somebody with somebody.The lower end of vertical tube and the threaded upper ends of outlet pipe are detachably connected, and benefit is for ease of overhauling and change in box body
Pellet nanoparticle material.
Further, multiple inlet openings are uniformly arranged on the bottom wall of the nanoparticle box, each inlet opening
A diameter of 3-8mm.
Further, the nanoparticle box is rectangular-shape.
Further, the cyclone main body, cutting thorn, cruciform joint and nanoparticle box are made by ABS plastic.
Further, the cyclone main body, cutting thorn and cruciform joint are integrally formed by ABS plastic.
Further, the particle diameter of the pellet nanoparticle material be 4-12mm and its be more than the inlet opening diameter.
Further, the cumulative volume of the pellet nanoparticle material of the accumulation in the nanoparticle box accounts for described hollow
The 75-90% of cavity volume.The cumulative volume of pellet nanoparticle material only accounts for the 75-90% of hollow cavity volume, and purpose is to keep away
Exempting from accumulation too closely makes water be not easy to be inhaled into, and the nanoparticle material of each pellet rushes in current after fluff packing
Have certain freedom of movement under brush, collision and rubbing action in activity collision and current is gradually taken away part ion material
Material, to reach its purpose with ozone contact in gas.
Further, the pellet nanoparticle material by negative ion powder, ozone activation catalyst, solid slow-release demulsifier and
Gel is combined.Solid slow-release demulsifier can slowly discharge demulsifier in current scour, with beneficial to the profit in waste water point
From.
Each component in pellet nanoparticle material is commercially available prod, and negative ion powder contains in pellet nanoparticle material
It is 40-50wt% to measure as 40-50wt%, ozone activation catalyst content, and the content of solid slow-release demulsifier is 5-8wt%, is coagulated
The content of glue is 5-10wt%.Wherein, ozone activation catalyst is load type metal catalyst, metal oxide catalyst or work
Property Pd/carbon catalyst, is briefly described by taking activated carbon as an example, activated carbon not only have to ozone certain adsorption capacity (reduce its from
Directly overflowed in water), and ozone it is adsorbed after under activated carbon effect its can accelerate to be transformed into hydroxyl radical free radical, so as to improve
Oxidation efficiency；Solid slow-release demulsifier by the metal oxides such as aluminum oxide, zinc oxide, cupric oxide it is compound after handle through overcure,
Then solid slow-release demulsifier is added again into (solid slow-release demulsifier is triumphant by Wuxi Ronghe Environmental Protection Equipment Co., Ltd. or Wuxi
En Kete renewable sources of energy Science and Technology Ltd. produces)；Gel is preferably the good silicon gel of adhesive property.
Compared with prior art, the beneficial effects of the invention are as follows：The aerator includes nanoparticle box, accumulation in it
Pellet nanoparticle material, during aeration water by nanoparticle cassette bottom portion or the inlet opening of side wall enter in box body with pellet nanometer from
Sub- material, the anion of pellet nanoparticle material release can be taken away in contact process and takes away the part pellet nanometer
Ionic material, then enter with together with the air, ozone and negative oxygen ion of air inlet mouth of pipe entrance in cyclone main body, in ozone and water
The part pellet nanoparticle material of carrying is simultaneously changed into the stronger hydroxyl radical free radical of oxidability by catalytic activation, improves
The content of ozone, anion and hydroxyl radical free radical in waste water, so as to greatly strengthening wastewater purification efficiency.
Brief description of the drawings
Fig. 1 is a kind of structural representation of nanoparticle rotational flow aeration device provided by the invention；
Fig. 2 is the cyclone main body of the nanoparticle rotational flow aeration device shown in Fig. 1 and the schematic top plan view for cutting thorn thereon；
Fig. 3 is the structural representation of the nanoparticle box of the nanoparticle rotational flow aeration device shown in Fig. 1.
In accompanying drawing, the list of parts representated by each label is as follows：
1. cyclone main body；2. cruciform joint；3. nanoparticle box；101. cutting thorn；102. spiral organ；103. through hole；
201. transverse tube；202. vertical tube；301. outlet pipe；302. inlet opening；1011. the body of rod；1012. cutting sheet.
Embodiment
The principle and feature of the present invention are described below in conjunction with drawings and the specific embodiments, example is served only for solving
The present invention is released, is not intended to limit the scope of the present invention.
As shown in Figures 1 to 3, the present invention provides a kind of nanoparticle rotational flow aeration device, and it includes cyclone main body 1, cross joint
First 2 and nanoparticle box 3, the cyclone main body 1 is described to be vertically arranged barrel-shaped, the open top of the cyclone main body 1
Through hole 103 is offered in the middle part of the bottom wall of cyclone main body 1, cutting thorn 101 and spiral organ 102 are provided with the cyclone main body 1, it is described
Spiral organ 102 be arranged at it is described cutting thorn 101 lower section, the nanoparticle box 3 have hollow cavity and its top be provided with
The outlet pipe 301 of the hollow cavity connection, the interior accumulation of the hollow cavity have capable of releasing negative ion and catalytic activation ozone
Pellet nanoparticle material, the bottom wall and/or side wall of the nanoparticle box 3 offer multiple inlet openings 302, the cross joint
First 2 are crossed as cross and interconnected to form by a vertical tube 202 and a transverse tube 201, the upper end of the vertical tube 202 with it is described
Through hole 103 is connected, and the lower end of the vertical tube 202 is connected with the upper end of the outlet pipe 301, the both ends difference of the transverse tube 201
For air inlet mouth of pipe and outlet mouth of pipe, the air inlet mouth of pipe is connected by upstream inlet pipe with air blower, and the upstream inlet pipe is also
Connected respectively with ozone generating-device and negative oxygen ion generating means, downstream is closed or passed through to the outlet mouth of pipe by sealing-plug
Air inlet pipe connects with the air inlet mouth of pipe of nanoparticle rotational flow aeration device another described.
Each component in pellet nanoparticle material is commercially available prod, and negative ion powder contains in pellet nanoparticle material
It is 40-50wt% to measure as 40-50wt%, ozone activation catalyst content, and the content of solid slow-release demulsifier is 5-8wt%, is coagulated
The content of glue is 5-10wt%.Wherein, negative ion powder be human use's nature produce anion principle, it is artificial synthesized or
A kind of complex mineral of proportioning, typically tourmaline powder+lanthanide series or rare earth element, its rare earth elements are matched somebody with somebody frequently
Example greatly exceed tourmaline powder, and rare earth has accounted for more than 60%；Ozone activation catalyst is load type metal catalyst, metal
Oxide catalyst or activated-carbon catalyst, are briefly described by taking activated carbon as an example, and activated carbon not only has certain to ozone
Adsorption capacity (reduce its from water directly overflow), and ozone it is adsorbed after under activated carbon effect its can accelerate to be transformed into hydroxyl
Base free radical, so as to improve oxidation efficiency；Solid slow-release demulsifier is answered by metal oxides such as aluminum oxide, zinc oxide, cupric oxide
Handled after conjunction through overcure, then add solid slow-release demulsifier again into (solid slow-release demulsifier is set by Wuxi is flourish with environmental protection
Standby Co., Ltd or Wuxi Kai'en Kete Renewable Energy Technology Co., Ltd. produce)；Gel is preferably good organic of adhesive property
Silica hydrogel.The preparation method of pellet nanoparticle material is：After first each component except gel is weighed in parts by weight, milling
Processing, is milled to 0.001 μm or so of average grain diameter, then adds gel and is stirred, pellet particle is made in pellet processing machine, i.e.,
.
Further, the cutting thorn 101 is multiple bodies of rod that uniform intervals are set in the inwall circumference of cyclone main body 1
1011, radial direction of the body of rod 1011 along the cyclone main body 1 stretches, one end of the body of rod 1011 and the eddy flow master
The inwall of body 1 is fixedly connected, the other end close to the cyclone main body 1 central axis, on each body of rod 1011 uniformly between
Every being provided with cutting sheet 1012, each cutting sheet 1012 is vertically set.
Further, the lower end of the vertical tube 202 is provided with external screw thread, and the upper end of the outlet pipe 301 is provided with and the outer spiral shell
The internal thread that line matches.
Further, multiple inlet openings 302 are uniformly arranged on the bottom wall of the nanoparticle box 3, it is each described enter
A diameter of 3-8mm in water hole 302.
Further, the nanoparticle box 3 is rectangular-shape.
Further, the cyclone main body 1, cutting thorn 101, cruciform joint 2 and nanoparticle box 3 are made by ABS plastic.
Further, the cyclone main body 1, cutting thorn 101 and cruciform joint 2 are integrally formed by ABS plastic.
Further, the particle diameter of the pellet nanoparticle material be 4-12mm and its be more than the inlet opening 302 diameter.
Further, the cumulative volume of the pellet nanoparticle material of the accumulation in the nanoparticle box 3 account for it is described in
The 75-90% of cavity body volume.
Further, the pellet nanoparticle material by negative ion powder, ozone activation catalyst, solid slow-release demulsifier and
Gel is combined.
The foregoing is only presently preferred embodiments of the present invention, be not intended to limit the invention, it is all the present invention spirit and
Within principle, any modification, equivalent substitution and improvements made etc., it should be included in the scope of the protection.
Claims (10)
1. a kind of nanoparticle rotational flow aeration device, it is characterised in that including cyclone main body (1), cruciform joint (2) and nanoparticle
Box (3), the cyclone main body (1) are to be vertically arranged barrel-shaped, the open top of the cyclone main body (1), the eddy flow master
Through hole (103) is offered in the middle part of the bottom wall of body (1), cutting thorn (101) and spiral organ (102) are provided with the cyclone main body (1),
The spiral organ (102) be arranged at it is described cutting thorn (101) lower section, the nanoparticle box (3) have hollow cavity and its
Top is provided with the outlet pipe (301) connected with the hollow cavity, and being accumulated in the hollow cavity has capable of releasing negative ion and urge
Change the pellet nanoparticle material of activated ozone, the bottom wall and/or side wall of the nanoparticle box (3) offer multiple inlet openings
(302), the cruciform joint (2) is crossed as cross and interconnected to form by a vertical tube (202) and a transverse tube (201),
The upper end of the vertical tube (202) is connected with the through hole (103), lower end and the outlet pipe (301) of the vertical tube (202)
Upper end connects, and the both ends of the transverse tube (201) are respectively air inlet mouth of pipe and outlet mouth of pipe, and the air inlet mouth of pipe passes through upstream inlet
Pipe connects with air blower, and the upstream inlet pipe also connects with ozone generating-device and negative oxygen ion generating means respectively, described
Outlet mouth of pipe is closed by sealing-plug or by downstream inlet pipe with entering described in nanoparticle rotational flow aeration device another described
Gas tube orifice connects.
2. a kind of nanoparticle rotational flow aeration device according to claim 1, it is characterised in that the cutting pierces (101) and is
In multiple bodies of rod (1011) that the circumferentially upper uniform intervals of the cyclone main body (1) inwall are set, the body of rod (1011) is along described
The radial direction stretching, extension of cyclone main body (1), one end of the body of rod (1011) is fixed with the inwall of the cyclone main body (1) to be connected
Connect, the other end is close to the central axis of the cyclone main body (1), and each uniform intervals are provided with cutting on the body of rod (1011)
Piece (1012), each cutting sheet (1012) are vertically set.
3. a kind of nanoparticle rotational flow aeration device according to claim 1, it is characterised in that under the vertical tube (202)
End is provided with external screw thread, and the upper end of the outlet pipe (301) is provided with the internal thread to match with the external screw thread.
A kind of 4. nanoparticle rotational flow aeration device according to claim 1, it is characterised in that multiple inlet openings
(302) it is uniformly arranged on the bottom wall of the nanoparticle box (3), a diameter of 3-8mm of each inlet opening (302).
A kind of 5. nanoparticle rotational flow aeration device according to claim 1, it is characterised in that the nanoparticle box (3)
For rectangular-shape.
6. a kind of nanoparticle rotational flow aeration device according to claim 1, it is characterised in that the cyclone main body (1), cut
Thorn (101), cruciform joint (2) and nanoparticle box (3) is cut to be made by ABS plastic.
7. a kind of nanoparticle rotational flow aeration device according to claim 6, it is characterised in that the cyclone main body (1), cut
Cut thorn (101) and cruciform joint (2) is integrally formed by ABS plastic.
A kind of 8. nanoparticle rotational flow aeration device according to claim 1, it is characterised in that the pellet nanoparticle material
The particle diameter of material be 4-12mm and its be more than the inlet opening (302) diameter.
A kind of 9. nanoparticle rotational flow aeration device according to claim 1, it is characterised in that the nanoparticle box (3)
The cumulative volume of the pellet nanoparticle material of interior accumulation accounts for the 75-90% of the hollow cavity volume.
A kind of 10. nanoparticle rotational flow aeration device according to any one of claim 1 to 9, it is characterised in that the pellet
Nanoparticle material is combined by negative ion powder, ozone activation catalyst, solid slow-release demulsifier and gel.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201710907106.3A CN107500398A (en) | 2017-09-29 | 2017-09-29 | A kind of nanoparticle rotational flow aeration device |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201710907106.3A CN107500398A (en) | 2017-09-29 | 2017-09-29 | A kind of nanoparticle rotational flow aeration device |
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| Publication Number | Publication Date |
|---|---|
| CN107500398A true CN107500398A (en) | 2017-12-22 |
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| CN201710907106.3A Pending CN107500398A (en) | 2017-09-29 | 2017-09-29 | A kind of nanoparticle rotational flow aeration device |
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2017
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| 周柏青: "《电厂化学》", 北京：中国电力出版社, pages: 43 - 44 * |
| 孙鹏: "臭氧催化氧化技术的应用", 《化工管理》, no. 19, 31 July 2017 (2017-07-31), pages 55 * |
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