CN108554703A - Enhance the method for photocatalyst atomization diffusion - Google Patents
Enhance the method for photocatalyst atomization diffusion Download PDFInfo
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- CN108554703A CN108554703A CN201810353794.8A CN201810353794A CN108554703A CN 108554703 A CN108554703 A CN 108554703A CN 201810353794 A CN201810353794 A CN 201810353794A CN 108554703 A CN108554703 A CN 108554703A
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- Prior art keywords
- photocatalyst
- atomization
- electromagnetic pump
- enhancing
- diffusion
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Classifications
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B05—SPRAYING OR ATOMISING IN GENERAL; APPLYING FLUENT MATERIALS TO SURFACES, IN GENERAL
- B05B—SPRAYING APPARATUS; ATOMISING APPARATUS; NOZZLES
- B05B17/00—Apparatus for spraying or atomising liquids or other fluent materials, not covered by the preceding groups
- B05B17/04—Apparatus for spraying or atomising liquids or other fluent materials, not covered by the preceding groups operating with special methods
- B05B17/06—Apparatus for spraying or atomising liquids or other fluent materials, not covered by the preceding groups operating with special methods using ultrasonic or other kinds of vibrations
Abstract
The present invention relates to a kind of methods of enhancing photocatalyst atomization diffusion, leafing agent smog is generated using heating to circulate in stainless steel tube, and with photocatalyst solution heat exchange, circulating-heating, to reach 40 DEG C 50 DEG C of photocatalyst atomization temperature, again under ultrasonic unit concussion, Photocatalyst water solution is fully atomized, and is spread；Swirling eddy is recycled to drive atomization photocatalyst rotational flow, atomization photocatalyst is with Diffusion of gas stream, and diffusion is uniform, and diffusivity is strong, range is wide, enhances the diffusivity of photocatalyst.
Description
Technical field
The present invention relates to photocatalyst fields, and in particular to a method of enhancing photocatalyst atomization diffusion.
Background technology
Photocatalyst series nanometer grade material, Photocatalyst water solution are that nanometer mountain flour is dissolved in water by special formula.
Less than 20 DEG C, with ultrasonic unit, it cannot be made fully to be atomized.Photocatalyst water solution ultrasonic wave
Device, atomization optimum temperature are 40 DEG C -50 DEG C, and due to the specific properties of photocatalyst, in order to make atomization temperature reach 40 DEG C -50
DEG C, the unavailable electromagnetic heating of mode of heating (cannot be by electromagnetic interference), unavailable electrothermal tube heating.
Due to photocatalyst system nanometer mountain flour aqueous solution, during ultrasonic atomization, the diffusion energy force difference of photocatalyst, diffusion
Range is small and uneven, cause far from equipment place diffusion less than.
Invention content
To solve the above problems, the present invention proposes a kind of method of enhancing photocatalyst atomization diffusion, it is skillfully constructed, photocatalyst
Atomizing effect is good, and spreads uniformly, and diffusivity is strong, range is wide.
Technical scheme of the present invention：
A method of enhancing photocatalyst atomization diffusion carries out Photocatalyst water solution by enhanced diffustion type photocatalyst atomizer
Atomization diffusion, the enhanced diffustion type photocatalyst atomizer includes photocatalyst chemical tank, it is characterised in that：It uses leafing agent
Smog contacts with the swirling eddy that air mixing generates and drives atomization photocatalyst diffusion；The leafing agent heating sublimation is formed
Leafing agent smog is sent by wind turbine in photocatalyst chemical tank；The photocatalyst chemical tank includes seal case, top of the box
Aerosol outlet port is set, and babinet side is provided with air inlet, and air inlet side is provided with sloping baffle in babinet, and baffle top is solid
Surely connect top of the box, bottom is tilted to air inlet side, baffle plate face face air inlet, between baffle and box bilateral wall there are
Gap, the bottom of box are additionally provided with supersonic generator；The wind turbine gas outlet is connected to the air inlet of photocatalyst chemical tank.
Photocatalyst aqueous solution is injected in photocatalyst chemical tank, and is heated to 40-50 DEG C, starts supersonic generator and shakes light
Catalyst aqueous solution generates atomization photocatalyst, while the mixing smog that leafing agent smog is mixed with air is sent into light by air inlet
In catalyst chemical tank, mixing smog hit sloping baffle after, leafing agent is uniformly dispersed, at the same sloping baffle force mixing smog from
Two side runner of baffle, and then swirling eddy is generated, swirling eddy, which contact and driven, is atomized photocatalyst long range diffusion, and from smog
It sends out outlet；
Above-mentioned technical proposal is improved further and is refined, the enhanced diffustion type photocatalyst atomizer further includes electric appliance
Control cabinet, electric appliance control box side wall are provided with ventilation hole, and showy medicament pot, wind turbine, the first electromagnetism are provided in electric appliance control box
Pump, the second electromagnetic pump, primary heater and secondary heater, fan outlet are connected to air inlet, and the medicament pot that floats passes through first
Electromagnetic pump is connected to primary heater, and primary heater is connected at fan outlet, and the medicament pot that floats passes through the second electromagnetic pump connection the
Two heaters, secondary heater are connected to stainless steel tube one end, and stainless steel tube passes through the showy medicament pot of stainless steel tube other end connection,
Circulating-heating circuit is formed, is provided with control panel on the electric appliance control box, control panel is electrically connected wind turbine, the first electromagnetism
Pump, the second electromagnetic pump, primary heater, secondary heater, supersonic generator and power interface, power interface are arranged in electricity
Babinet side is controlled, power interface connects external power supply, and the stainless steel tube is uniformly arranged on photocatalyst chemical tank bottom.
Start the second electromagnetic pump, secondary heater, leafing agent is pumped into secondary heater via the second electromagnetism and heats, heating
The leafing agent smog of generation is added by stainless steel tube by the Photocatalyst water solution heat exchange in coil pipe and photocatalyst chemical tank
Hot Photocatalyst water solution, and leafing agent after cooling is sending showy medicament pot back to, circulating-heating, realizes the heating of Photocatalyst water solution
Purpose.
Start wind turbine, the first electromagnetic pump, the second electromagnetic pump, leafing agent is pumped into primary heater via the first electromagnetism and adds
The leafing agent smog of heat, generation is sent at fan outlet, and the air extracted with wind turbine mixes and by being sent into photocatalyst together with wind turbine
Chemical tank.
Above-mentioned technical proposal is improved further and is refined, the leafing agent is diethylene glycol (DEG) aqueous solution.
Above-mentioned technical proposal is improved further and is refined, the diethylene glycol (DEG) aqueous solution is by diethylene glycol (DEG) and pure water
According to weight ratio 1：3 are mixed.
Above-mentioned technical proposal is improved further and is refined, diethylene glycol (DEG) aqueous solution and the weight with Photocatalyst water solution
Ratio is 0.4-0.5Kg：3Kg.
Above-mentioned technical proposal is improved further and is refined, rate of discharge and the primary heater of the first electromagnetic pump add
Hot temperature is set according to the nebulization efficiency of leafing agent, and leafing agent enters primary heater by the first electromagnetic pump and is atomized completely, is led to
It crosses and is precisely controlled, effectively prevent entering photocatalyst chemical tank for the leafing agent not being atomized, impact.
Above-mentioned technical proposal is improved further and is refined, the heating of the primary heater, secondary heater
Temperature setting is 100-143 DEG C, and diethylene glycol (DEG) heating reaches 100 DEG C or more and is atomized, and the flash temperature of diethylene glycol (DEG) is 143 DEG C, flash-point
The safety index for being flammable liquid storage, transporting and using.
The benefit that the present invention generates：Leafing agent smog is generated using heating to circulate in stainless steel tube, and is touched with light
Matchmaker's solution heat exchange, circulating-heating, to reach 40 DEG C -50 DEG C of photocatalyst atomization temperature；Atomization light is driven using swirling eddy
Catalyst rotational flow, atomization photocatalyst is with Diffusion of gas stream, and diffusion is uniform, and diffusivity is strong, range is wide, enhances photocatalyst
Diffusivity.
Description of the drawings
Fig. 1 is the flow diagram for the method for enhancing photocatalyst atomization diffusion.
Fig. 2 is enhanced diffustion type photocatalyst atomizer structure schematic diagram in embodiment 1.
Fig. 3 is enhanced diffustion type photocatalyst atomizer half-section diagram in embodiment 1.
01 wind turbine 07 of photocatalyst chemical tank floats 02 first electromagnetic pump of medicament pot, 03 second electromagnetic pump 05 in figure
One heater, 04 secondary heater 06.
Specific implementation mode
As shown in Figs. 1-3, a method of enhancing photocatalyst atomization diffusion passes through enhanced diffustion type photocatalyst atomizer pair
Photocatalyst water solution carries out atomization diffusion, and the enhanced diffustion type photocatalyst atomizer includes photocatalyst chemical tank 01, it is adopted
It is contacted with the swirling eddy that air mixing generates with diethylene glycol (DEG) smog and drives atomization photocatalyst diffusion；The diethylene glycol (DEG) is water-soluble
Liquid heating sublimation forms diethylene glycol (DEG) smog, is sent into photocatalyst chemical tank 01 by wind turbine 07；The photocatalyst chemical tank 01
Including seal case, aerosol outlet port is arranged in top of the box, and babinet side is provided with air inlet, and air inlet side is arranged in babinet
There are sloping baffle, baffle top to be fixedly connected with top of the box, bottom is tilted to air inlet side, baffle plate face face air inlet, gear
There are gaps, the bottom of box to be additionally provided with supersonic generator between plate and box bilateral wall；The wind turbine gas outlet and light
The air inlet of catalyst chemical tank is connected to.
Photocatalyst aqueous solution is injected in photocatalyst chemical tank 01, and is heated to 40-50 DEG C, starts supersonic generator concussion
Photocatalyst water solution generates atomization photocatalyst, while the mixing smog that diethylene glycol (DEG) smog is mixed with air is sent by air inlet
In photocatalyst chemical tank 01, after mixing smog hits sloping baffle, pure water is uniformly dispersed, while sloping baffle forces mixing cigarette
Mist generates swirling eddy from two side runner of baffle, and swirling eddy, which is contacted and driven, is atomized photocatalyst long range diffusion, and from
Aerosol outlet port is sent out.
The diethylene glycol (DEG) aqueous solution is by diethylene glycol (DEG) and pure water according to weight ratio 1：3 are mixed；Diethylene glycol (DEG) aqueous solution
With with the weight ratio of Photocatalyst water solution be 0.4-0.5Kg：3Kg.
The enhanced diffustion type photocatalyst atomizer further includes electric appliance control box, and electric appliance control box side wall is provided with ventilation
Hole is provided with showy medicament pot 02, wind turbine 07, the first electromagnetic pump 03, the second electromagnetic pump 05, primary heater in electric appliance control box
04 and secondary heater 06,07 outlet air inlet of wind turbine, the medicament pot 02 that floats passes through the first electromagnetic pump 03 connection first
Heater 04, primary heater 04 are connected to 07 exit of wind turbine, and the medicament pot 02 that floats is added by the second electromagnetic pump 05 connection second
Hot device 06, secondary heater 06 are connected to stainless steel tube one end, and stainless steel tube passes through the showy medicament pot of stainless steel tube other end connection
02, circulating-heating circuit is formed, is provided with control panel on the electric appliance control box, control panel is electrically connected wind turbine 07, the
One electromagnetic pump 03, the second electromagnetic pump 05, primary heater 04, secondary heater 06, supersonic generator and power interface, electricity
Source interface setting connects external power supply in electronic-control box side, power interface, and the stainless steel tube is uniformly arranged on photocatalyst
01 bottom of chemical tank；The rate of discharge of first electromagnetic pump 03 is with 04 heating temperature of primary heater according to the nebulization efficiency of pure water
Setting, pure water enter primary heater 04 by the first electromagnetic pump 03 and are atomized completely, by being precisely controlled, effectively prevent as not
The pure water of atomization enters photocatalyst chemical tank, impacts.
Due to the finiteness of literal expression, and objectively there is unlimited concrete structure, for the common of the art
For technical staff, without departing from the principle of the present invention, several improvement, retouching or variation can also be made, it can also
Above-mentioned technical characteristic is combined in the right way；These improve retouching, variation or combination, or not improved by invention
Design and technical solution directly apply to other occasions, are regarded as protection scope of the present invention.
Claims (7)
1. it is a kind of enhancing photocatalyst atomization diffusion method, by enhanced diffustion type photocatalyst atomizer to Photocatalyst water solution into
Row atomization diffusion, the enhanced diffustion type photocatalyst atomizer includes photocatalyst chemical tank, it is characterised in that：It is using floating
Agent smog contacts with the swirling eddy that air mixing generates and drives atomization photocatalyst diffusion；The leafing agent heating sublimation shape
At leafing agent smog, it is sent into photocatalyst chemical tank by wind turbine；The photocatalyst chemical tank includes seal case, babinet top
Aerosol outlet port is arranged in portion, and babinet side is provided with air inlet, and air inlet side is provided with sloping baffle, baffle top in babinet
It is fixedly connected with top of the box, bottom is tilted to air inlet side, and baffle plate face face air inlet stays between baffle and box bilateral wall
There are gap, the bottom of box to be additionally provided with supersonic generator；The wind turbine gas outlet and the air inlet of photocatalyst chemical tank connect
It is logical；
Photocatalyst aqueous solution is injected in photocatalyst chemical tank, and is heated to 40-50 DEG C, starts supersonic generator and shakes photocatalyst
Aqueous solution generates atomization photocatalyst, while the mixing smog that leafing agent smog is mixed with air is sent into photocatalyst by air inlet
In chemical tank, after mixing smog hits sloping baffle, leafing agent is uniformly dispersed, while sloping baffle forces mixing smog from baffle
Two side runners, and then swirling eddy is generated, swirling eddy, which contact and driven, is atomized photocatalyst long range diffusion, and from aerosol outlet port
It sends out.
2. a kind of method of enhancing photocatalyst atomization diffusion according to claim 1, it is characterised in that：The enhancing is expanded
It further includes electric appliance control box to dissipate type photocatalyst atomizer, and electric appliance control box side wall is provided with ventilation hole, is arranged in electric appliance control box
There are showy medicament pot, wind turbine, the first electromagnetic pump, the second electromagnetic pump, primary heater and secondary heater, fan outlet connection
Air inlet, the medicament pot that floats are connected to primary heater by the first electromagnetic pump, and primary heater is connected at fan outlet, and float medicine
Agent pot is connected to secondary heater by the second electromagnetic pump, and secondary heater is connected to stainless steel tube one end, and stainless steel tube passes through stainless
The showy medicament pot of steel pipe other end connection, forms circulating-heating circuit, control panel is provided on the electric appliance control box, control
Plate be electrically connected wind turbine, the first electromagnetic pump, the second electromagnetic pump, primary heater, secondary heater, supersonic generator and
Power interface, power interface setting connect external power supply in electronic-control box side, power interface, and the stainless steel tube is uniformly set
It sets in photocatalyst chemical tank bottom.
3. a kind of method of enhancing photocatalyst atomization diffusion according to claim 2, it is characterised in that：The leafing agent
For diethylene glycol (DEG) aqueous solution.
4. a kind of method of enhancing photocatalyst atomization diffusion according to claim 3, it is characterised in that：The diethylene glycol (DEG)
Aqueous solution is by diethylene glycol (DEG) and pure water according to weight ratio 1：3 are mixed.
5. a kind of method of enhancing photocatalyst atomization diffusion according to claim 3, it is characterised in that：Diethylene glycol (DEG) aqueous solution
With with the weight ratio of Photocatalyst water solution be 0.4-0.5Kg：3Kg.
6. a kind of method of enhancing photocatalyst atomization diffusion according to claim 5, it is characterised in that：First electromagnetic pump
Rate of discharge is set with primary heater heating temperature according to the nebulization efficiency of leafing agent, and leafing agent enters by the first electromagnetic pump
Primary heater is atomized completely.
7. a kind of method of enhancing photocatalyst atomization diffusion according to claim 6, it is characterised in that：Described
Primary heater, secondary heater heating temperature be set as 100-143 DEG C.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201810353794.8A CN108554703A (en) | 2018-04-19 | 2018-04-19 | Enhance the method for photocatalyst atomization diffusion |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201810353794.8A CN108554703A (en) | 2018-04-19 | 2018-04-19 | Enhance the method for photocatalyst atomization diffusion |
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| Publication Number | Publication Date |
|---|---|
| CN108554703A true CN108554703A (en) | 2018-09-21 |
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ID=63535901
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201810353794.8A Pending CN108554703A (en) | 2018-04-19 | 2018-04-19 | Enhance the method for photocatalyst atomization diffusion |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109801546A (en) * | 2019-01-30 | 2019-05-24 | 嘉兴市天篷农业休闲有限公司 | A kind of smoke head and the aerosol producer for Long March experience using the smoke head |
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| JPH07151108A (en) * | 1993-08-03 | 1995-06-13 | Bdag Balcke Duerr Ag | Piffuser |
| JP2002001183A (en) * | 2000-06-15 | 2002-01-08 | Omron Corp | Ultrasonic atomizing device |
| CN1695031A (en) * | 2002-12-03 | 2005-11-09 | Lg电子株式会社 | Flow spreading mechanism |
| WO2009013843A1 (en) * | 2007-07-24 | 2009-01-29 | Konishi Seiko Co., Ltd. | Portable ultrasonic mist generating device |
| CN206046361U (en) * | 2016-08-31 | 2017-03-29 | 吕琳 | A kind of ultrasonic atomizing sterilizer |
| CN107735184A (en) * | 2015-05-28 | 2018-02-23 | 首尔大学校产学协办团 | Ultra micron sprayer unit |
-
2018
- 2018-04-19 CN CN201810353794.8A patent/CN108554703A/en active Pending
Patent Citations (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4151955A (en) * | 1977-10-25 | 1979-05-01 | Bowles Fluidics Corporation | Oscillating spray device |
| CN2078199U (en) * | 1990-06-15 | 1991-06-05 | 蒋隽 | Multipurpose protable ultrasonic atomizer |
| JPH07151108A (en) * | 1993-08-03 | 1995-06-13 | Bdag Balcke Duerr Ag | Piffuser |
| JP2002001183A (en) * | 2000-06-15 | 2002-01-08 | Omron Corp | Ultrasonic atomizing device |
| CN1695031A (en) * | 2002-12-03 | 2005-11-09 | Lg电子株式会社 | Flow spreading mechanism |
| WO2009013843A1 (en) * | 2007-07-24 | 2009-01-29 | Konishi Seiko Co., Ltd. | Portable ultrasonic mist generating device |
| CN107735184A (en) * | 2015-05-28 | 2018-02-23 | 首尔大学校产学协办团 | Ultra micron sprayer unit |
| CN206046361U (en) * | 2016-08-31 | 2017-03-29 | 吕琳 | A kind of ultrasonic atomizing sterilizer |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109801546A (en) * | 2019-01-30 | 2019-05-24 | 嘉兴市天篷农业休闲有限公司 | A kind of smoke head and the aerosol producer for Long March experience using the smoke head |
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Application publication date: 20180921 |
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| RJ01 | Rejection of invention patent application after publication |