WO2021218052A1 - Mixer and separated air purification device comprising same - Google Patents

Mixer and separated air purification device comprising same Download PDF

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Publication number
WO2021218052A1
WO2021218052A1 PCT/CN2020/121480 CN2020121480W WO2021218052A1 WO 2021218052 A1 WO2021218052 A1 WO 2021218052A1 CN 2020121480 W CN2020121480 W CN 2020121480W WO 2021218052 A1 WO2021218052 A1 WO 2021218052A1
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Prior art keywords
mixer
air
fluid
inlet
liquid storage
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PCT/CN2020/121480
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French (fr)
Chinese (zh)
Inventor
龙新平
程怀玉
许霜杰
季斌
唐巾洁
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武汉大学
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Publication of WO2021218052A1 publication Critical patent/WO2021218052A1/en

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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D53/00Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/14Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by absorption
    • B01D53/1487Removing organic compounds
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D47/00Separating dispersed particles from gases, air or vapours by liquid as separating agent
    • B01D47/02Separating dispersed particles from gases, air or vapours by liquid as separating agent by passing the gas or air or vapour over or through a liquid bath
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F23/00Mixing according to the phases to be mixed, e.g. dispersing or emulsifying
    • B01F23/20Mixing gases with liquids
    • B01F23/23Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids
    • B01F23/232Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids using flow-mixing means for introducing the gases, e.g. baffles
    • B01F23/2326Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids using flow-mixing means for introducing the gases, e.g. baffles adding the flowing main component by suction means, e.g. using an ejector
    • AHUMAN NECESSITIES
    • A61MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61LMETHODS OR APPARATUS FOR STERILISING MATERIALS OR OBJECTS IN GENERAL; DISINFECTION, STERILISATION OR DEODORISATION OF AIR; CHEMICAL ASPECTS OF BANDAGES, DRESSINGS, ABSORBENT PADS OR SURGICAL ARTICLES; MATERIALS FOR BANDAGES, DRESSINGS, ABSORBENT PADS OR SURGICAL ARTICLES
    • A61L9/00Disinfection, sterilisation or deodorisation of air
    • A61L9/14Disinfection, sterilisation or deodorisation of air using sprayed or atomised substances including air-liquid contact processes
    • A61L9/145Disinfection, sterilisation or deodorisation of air using sprayed or atomised substances including air-liquid contact processes air-liquid contact processes, e.g. scrubbing
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D53/00Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/14Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by absorption
    • B01D53/1493Selection of liquid materials for use as absorbents
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D53/00Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/14Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by absorption
    • B01D53/18Absorbing units; Liquid distributors therefor
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F23/00Mixing according to the phases to be mixed, e.g. dispersing or emulsifying
    • B01F23/20Mixing gases with liquids
    • B01F23/23Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids
    • B01F23/232Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids using flow-mixing means for introducing the gases, e.g. baffles
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F25/00Flow mixers; Mixers for falling materials, e.g. solid particles
    • B01F25/30Injector mixers
    • B01F25/31Injector mixers in conduits or tubes through which the main component flows
    • B01F25/312Injector mixers in conduits or tubes through which the main component flows with Venturi elements; Details thereof
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F25/00Flow mixers; Mixers for falling materials, e.g. solid particles
    • B01F25/30Injector mixers
    • B01F25/31Injector mixers in conduits or tubes through which the main component flows
    • B01F25/312Injector mixers in conduits or tubes through which the main component flows with Venturi elements; Details thereof
    • B01F25/3124Injector mixers in conduits or tubes through which the main component flows with Venturi elements; Details thereof characterised by the place of introduction of the main flow
    • B01F25/31243Eductor or eductor-type venturi, i.e. the main flow being injected through the venturi with high speed in the form of a jet
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F25/00Flow mixers; Mixers for falling materials, e.g. solid particles
    • B01F25/30Injector mixers
    • B01F25/31Injector mixers in conduits or tubes through which the main component flows
    • B01F25/312Injector mixers in conduits or tubes through which the main component flows with Venturi elements; Details thereof
    • B01F25/3125Injector mixers in conduits or tubes through which the main component flows with Venturi elements; Details thereof characteristics of the Venturi parts
    • B01F25/31251Throats
    • B01F25/312512Profiled, grooved, ribbed throat, or being provided with baffles
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F25/00Flow mixers; Mixers for falling materials, e.g. solid particles
    • B01F25/30Injector mixers
    • B01F25/31Injector mixers in conduits or tubes through which the main component flows
    • B01F25/312Injector mixers in conduits or tubes through which the main component flows with Venturi elements; Details thereof
    • B01F25/3125Injector mixers in conduits or tubes through which the main component flows with Venturi elements; Details thereof characteristics of the Venturi parts
    • B01F25/31252Nozzles
    • B01F25/312522Profiled, grooved, ribbed nozzle, or being provided with baffles
    • AHUMAN NECESSITIES
    • A61MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61LMETHODS OR APPARATUS FOR STERILISING MATERIALS OR OBJECTS IN GENERAL; DISINFECTION, STERILISATION OR DEODORISATION OF AIR; CHEMICAL ASPECTS OF BANDAGES, DRESSINGS, ABSORBENT PADS OR SURGICAL ARTICLES; MATERIALS FOR BANDAGES, DRESSINGS, ABSORBENT PADS OR SURGICAL ARTICLES
    • A61L2209/00Aspects relating to disinfection, sterilisation or deodorisation of air
    • A61L2209/10Apparatus features
    • AHUMAN NECESSITIES
    • A61MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61LMETHODS OR APPARATUS FOR STERILISING MATERIALS OR OBJECTS IN GENERAL; DISINFECTION, STERILISATION OR DEODORISATION OF AIR; CHEMICAL ASPECTS OF BANDAGES, DRESSINGS, ABSORBENT PADS OR SURGICAL ARTICLES; MATERIALS FOR BANDAGES, DRESSINGS, ABSORBENT PADS OR SURGICAL ARTICLES
    • A61L2209/00Aspects relating to disinfection, sterilisation or deodorisation of air
    • A61L2209/20Method-related aspects
    • A61L2209/22Treatment by sorption, e.g. absorption, adsorption, chemisorption, scrubbing, wet cleaning
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D2247/00Details relating to the separation of dispersed particles from gases, air or vapours by liquid as separating agent
    • B01D2247/04Regenerating the washing fluid
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D2251/00Reactants
    • B01D2251/10Oxidants
    • B01D2251/108Halogens or halogen compounds
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D2251/00Reactants
    • B01D2251/60Inorganic bases or salts
    • B01D2251/602Oxides
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D2252/00Absorbents, i.e. solvents and liquid materials for gas absorption
    • B01D2252/10Inorganic absorbents
    • B01D2252/103Water
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D2252/00Absorbents, i.e. solvents and liquid materials for gas absorption
    • B01D2252/20Organic absorbents
    • B01D2252/202Alcohols or their derivatives
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D2257/00Components to be removed
    • B01D2257/70Organic compounds not provided for in groups B01D2257/00 - B01D2257/602
    • B01D2257/702Hydrocarbons
    • B01D2257/7027Aromatic hydrocarbons
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D2257/00Components to be removed
    • B01D2257/70Organic compounds not provided for in groups B01D2257/00 - B01D2257/602
    • B01D2257/708Volatile organic compounds V.O.C.'s
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D2257/00Components to be removed
    • B01D2257/91Bacteria; Microorganisms
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D2258/00Sources of waste gases
    • B01D2258/06Polluted air
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D2259/00Type of treatment
    • B01D2259/45Gas separation or purification devices adapted for specific applications
    • B01D2259/4508Gas separation or purification devices adapted for specific applications for cleaning air in buildings
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D47/00Separating dispersed particles from gases, air or vapours by liquid as separating agent
    • B01D47/02Separating dispersed particles from gases, air or vapours by liquid as separating agent by passing the gas or air or vapour over or through a liquid bath
    • B01D47/021Separating dispersed particles from gases, air or vapours by liquid as separating agent by passing the gas or air or vapour over or through a liquid bath by bubbling the gas through a liquid bath
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D47/00Separating dispersed particles from gases, air or vapours by liquid as separating agent
    • B01D47/10Venturi scrubbers

Definitions

  • At least one embodiment disclosed in the present invention relates to a mixer and a separate air purification device including the mixer.
  • the main components of indoor environmental pollutants are divided into the following four categories: PM2.5 suspended particulate matter, formaldehyde, nicotine and other volatile organic compounds, microorganisms, viruses, bacteria, and air odors.
  • the commonly used air purification technologies mainly include: light plasma technology, negative ion technology, photocatalyst technology, HEPA high-efficiency filtration technology, electrostatic dust collection technology and active oxygen technology.
  • the core components adopt filter screens or similar forms.
  • At least one embodiment disclosed in the present invention provides a mixer and a separate air purification device including the mixer. While ensuring energy saving, environmental protection and economy, the indoor air can be purified better.
  • At least one embodiment disclosed in the present invention provides a mixer, including: a first fluid inlet; a second fluid inlet; a suction chamber; a mixing pipe that mixes two fluids flowing in from the first fluid inlet and the second fluid inlet; And a diffuser that allows the mixed fluid to leave the mixer; the first fluid inlet is in fluid communication with the suction chamber through a nozzle, the second fluid inlet is in fluid communication with the suction chamber, the suction chamber, the mixing pipe In fluid communication with the diffuser tube in sequence, the flow channel area of the suction chamber gradually decreases along the fluid flow direction, the part of the mixing tube close to the suction chamber is a straight tube, and the mixing tube is far away from the The part of the suction chamber is a wavy pipe, and the flow channel area of the diffuser pipe gradually increases along the fluid flow direction.
  • a plurality of curved guide vanes are installed in the suction chamber, and the guide vanes extend from one end to the other end of the suction chamber.
  • the nozzle is a porous nozzle.
  • the nozzle is an orifice nozzle having an inverted cone shape to enhance the diffusion angle of the fluid.
  • the thickness of the deflector in the suction chamber is between 0.05D and 0.1D, and the height is between 0.1D and 0.2D, where D is the diameter of the mixing tube.
  • the length of the straight pipe in the mixing pipe is 3D to 5D, and the length of the wave-shaped pipe is between 12D and 20D, where D is the diameter of the mixing pipe.
  • the diffusion angle ⁇ of the diffusion tube is between 8 and 12°.
  • At least one embodiment disclosed in the present invention provides a separate indoor air purification device, including the mixer, a circulating water pump, a purified liquid storage tank, and an air suction port.
  • the tank body of the purified liquid storage tank has a filter chamber that filters out solid particles in the gas-liquid mixture flowing in through the gas-liquid mixture inlet, and a liquid storage chamber that stores the filtered purified liquid , wherein the gas-liquid mixture inlet is in fluid communication with the filter chamber, the purified liquid outlet is in fluid communication with the liquid storage chamber, and the air outlet is located above the liquid storage chamber and/or the filter chamber.
  • the air outlet and/or the air suction inlet on the purified liquid storage tank are provided with isolation nets.
  • Fig. 1 is a schematic cross-sectional structure diagram of a mixer provided by an embodiment of the present disclosure.
  • FIG. 2 is a schematic cross-sectional structure diagram of a mixer provided by another embodiment of the present disclosure.
  • Fig. 3a is a schematic structural diagram of a suction chamber with a rotating baffle provided by an embodiment of the present disclosure.
  • Fig. 3b is a schematic diagram of a partial structure of the suction chamber shown in Fig. 3a.
  • Fig. 4a is a front view of a porous nozzle provided by an embodiment of the present disclosure.
  • FIG. 4b is a schematic cross-sectional view of a porous nozzle provided by an embodiment of the present disclosure.
  • Fig. 5a is a front view of an orifice nozzle provided by an embodiment of the present disclosure.
  • Figure 5b is a schematic cross-sectional view of an orifice nozzle provided by an embodiment of the present disclosure.
  • Fig. 6 is a schematic diagram of the principle of a separation air purification device provided by an embodiment of the present disclosure.
  • FIG. 7 is a schematic diagram of the structure of a purification liquid storage tank provided by an embodiment of the present disclosure.
  • a type of mixer will be described, and the term "mixer” herein refers to a mixer that mixes fluids.
  • a mixer can mix air and purified liquid to produce a stream of purified air for environment or climate control.
  • the structure of the mixer is optimized.
  • the inside of the mixer will produce a very strong fluid shear mixing effect.
  • the inhaled air and the purified liquid will be fully mixed and chemically reacted to form a uniform gas-liquid mixture containing a large number of tiny bubbles.
  • the air and the purification The contact mixing of the liquid is very sufficient, which can maximize the air purification effect of the purification liquid.
  • Fig. 1 is a schematic cross-sectional structure diagram of a mixer provided by an embodiment of the present disclosure
  • Fig. 2 is a schematic cross-sectional structure diagram of a mixer provided by another embodiment of the present disclosure.
  • the mixer includes a first fluid inlet 1-1, a second fluid inlet 1-2, and a suction chamber 1-4, which will flow from the first fluid inlet 1-1 and the second fluid inlet 1-2
  • the mixing pipe 1-5 for mixing the two fluids, and the diffuser pipe 1-6 for the mixed fluid to leave the mixer.
  • the first fluid inlet 1-1 is in fluid communication with the suction chamber 1-4 through the nozzle 1-3, the nozzle 1-3 extends into the suction chamber 1-4, and the second fluid inlet 1-2 is in fluid communication with the suction chamber 1-4,
  • the suction chamber 1-4, the mixing pipe 1-5 and the diffusion pipe 1-6 are in fluid communication in sequence.
  • the pipe diameter of the suction chamber 1-4 gradually decreases along the fluid flow direction, and the pipe diameter of the diffuser pipe 1-6 gradually decreases along the fluid flow direction.
  • the part of the mixing pipe 1-5 close to the suction chamber 1-4 is a straight pipe
  • the part of the mixing pipe 1-5 far from the suction chamber 1-4 is a wavy pipe.
  • the fluid at the first fluid inlet 1-1 is the purified fluid with higher pressure after being pressurized
  • the fluid at the second fluid inlet 1-2 is the lower pressure
  • the flow channel area is reduced, forming multiple high-speed fluids, which enter the mixing pipe 1-5. Entrainment will form a low pressure zone at the mixing pipe 1-5. Under the effect of the pressure difference between the low pressure and the outside atmospheric pressure, the air to be purified is sucked into the mixer 1 and mixed with the purified liquid in the mixing pipe 1-5 , The gas-liquid mixture leaves the mixer through the diffuser 1-6.
  • the air and the purification liquid will be fully mixed in the mixing tube 1-5 to form a uniform gas-liquid mixture containing a large number of tiny bubbles, so that the air and the purification liquid can be fully mixed and reacted. Under the action of the purification liquid, a good Air purification effect. And because the mixer has a strong suction capacity for air, it can treat a large amount of contaminated air in a short time. In addition, the use of liquid-based purification fluids to treat air can simultaneously treat multiple types of pollutants, with strong universality and wide application scope.
  • a plurality of curved guide vanes are installed in the suction chamber 1-4, and the guide vanes extend from one end to the other end of the suction chamber 1-4.
  • the nozzles 1-3 can be porous nozzles 1-3a.
  • the porous nozzles 1-3a are arranged with multiple pore structures, which will transform the purification liquid from a single strand to multiple high-speed fluids.
  • the contact area with the air is increased, thereby significantly enhancing its ability to suck air, and is suitable for occasions that require high air purification speed.
  • nozzles 1-3 can also be orifice nozzles 1-3b, orifice nozzles 1-3b are inverted cones, which can greatly enhance the diffusion angle of the fluid flowing through the component, although Its mixing effect is slightly weaker than the porous nozzle 1-3a, but its flow loss is smaller, which is suitable for occasions where energy saving is more important.
  • the range of the main structural parameters of the mixer is defined.
  • the diameter D of the mixer mixing tube 1-5 is taken as the reference quantity.
  • the main structural parameters of the mixer can be: the inner diameter of the first fluid inlet 1-1 is about 1.2D ⁇ 1.5D; the inner diameter of the second fluid inlet 1-2 is about 2D ⁇ 4D; the distance between the nozzle 1-3 and the inlet of the mixing tube 1-5 The distance is about 0.7D ⁇ 1.5D, the diameter is about 0.3D ⁇ 0.6D; the thickness of the porous nozzle 1-3a is about 2.5mm ⁇ 5mm, the number of holes is 4 ⁇ 12, the size of each hole can be different, according to actual needs Adjust; the orifice diameter of the orifice nozzle 1-3b is about 0.15D ⁇ 0.45D, the thickness is about 2.5mm ⁇ 5mm, and the angle is 30° ⁇ 45°; the contraction angle ⁇ of the suction chamber 1-4 is 60° ⁇ Between 120
  • Fig. 6 is a schematic diagram of the principle of a separation air purification device provided by an embodiment of the present disclosure.
  • the separation type air purification device includes the mixer 1, the circulating water pump 2, the purified liquid storage tank 3 and the air suction port 5 as described above.
  • the circulating water pump 2 provides circulating power for the entire purification device, and its internal liquid contact surface has been specially treated (such as the use of PVC material to make the pump body, the pump surface is sprayed with anti-corrosion coating, etc.) to improve its corrosion resistance, and its Working noise is very small.
  • the air suction port 5 is a pipe with a horn-shaped end, which is placed in the environment to be purified and connected to the mixer 1 through the pipe. The main function is to introduce the air to be purified into the mixer 1.
  • the air suction port 5 can also be provided with an isolation net 6 to prevent some lighter sundries from being sucked into the mixer.
  • FIG. 7 is a schematic diagram of the structure of a purification liquid storage tank provided by an embodiment of the present disclosure.
  • the purified liquid storage tank 3 includes a tank body, and a gas-liquid mixture inlet 3-2, an air outlet 3-5 and a purified liquid outlet 3-6 located on the tank body.
  • the pre-prepared purification liquid 3-1 is installed in the tank, and its main components can be flexibly changed according to the specific conditions of indoor air pollutants to achieve the best purification effect.
  • the opening at the top of the box can be used as an air outlet 3-5.
  • a filter chamber and a liquid storage chamber can be provided in the tank body of the purified liquid storage tank 3.
  • the filter chamber is used to filter out solid particles in the gas-liquid mixture leaving the mixer 1, and the filtered purified liquid enters To the reservoir. Therefore, the filter chamber is in fluid communication with the gas-liquid mixture inlet 3-2, and the liquid storage chamber is in fluid communication with the air outlet 3-5 and the purified liquid outlet 3-6.
  • the filter chamber and the liquid storage chamber may be enclosed by the inner wall of the box body, the isolation plate 3-3, and the filter mesh 3-4.
  • the isolation board 3-3 is vertically arranged in the box.
  • the filter screen 3-4 is arranged horizontally, one side is connected with the isolation plate 3-3, and the other three sides are connected with the inner wall of the box.
  • the filter 3-4 can be detachable for easy cleaning.
  • a waste discharge port 3-7, a purification liquid stock replenishment device 3-8, and a water replenishment port 3-9 can also be provided on the purified liquid storage tank 3.
  • the waste outlet 3-7 is in fluid communication with the filter chamber, and the solid particles and waste liquid filtered by the filter mesh 3-4 can be discharged from the waste outlet 3-7 when the equipment is not working.
  • the purifying liquid stock replenishing device 3-8 can monitor the content of various purification active ingredients in the purified liquid in real time through the existing technology, and timely replenish the purified liquid stock to ensure the quality of the purified liquid 3-1 in the entire purification device.
  • An appropriate amount of water can be added to the purified liquid storage tank 3 through the water supply port 3-9 to compensate for the water consumption during the operation of the entire device.
  • the first fluid inlet 1-1 of the mixer 1 is in fluid communication with the purified fluid outlet 3-6 of the purified fluid storage tank 3 through the circulating water pump 2, and the second fluid inlet 1-2 of the mixer 1 is inhaled with air.
  • Port 5 is in fluid communication
  • the diffuser tube 1-6 of the mixer 1 is in fluid communication with the gas-liquid mixture inlet 3-2 on the purification liquid storage tank 3, and the pipe 7 between the diffuser tube 1-6 and the gas-liquid mixture inlet 3-2
  • the gas-liquid mixture leaving the mixer 1 enters the filter chamber inside the tank through the gas-liquid mixture inlet 3-2 on the purified liquid storage tank 3, and then passes through the filter screen 3-4.
  • the existing solid filtration further promotes the contact between the air and the purification liquid, which can improve the purification effect.
  • the gas-liquid mixture completes the gas-liquid separation in the tank, the purified air returns to the air through the air outlet 3-5, and the purified liquid enters the other side of the purified liquid storage tank 3 from the top of the isolation plate 3-3.
  • the liquid storage chamber enters the purification device pipeline from the purification liquid outlet 3-6 again to realize the recycling of the purification liquid.
  • a porous structure isolation net can be set at the air outlet 3-5.
  • a large-scale mixer 1 can be made to speed up the air purification rate, but in this way, violent air and purification liquid mixing will occur inside the mixer 1, resulting in strong noise.
  • the mixing The device 1 is alone outdoors, the remaining parts of the air purification device are indoors, and the parts are connected by pipes. If the mixer 1 is miniaturized, it can also be placed indoors.
  • the mixer 1 disclosed in the present invention is simple in structure, easy to manufacture, and reliable in operation, and other parts of the air purification device are relatively cheap, so the entire purification device is economical, reliable in operation, and easy to popularize.
  • the air purification device disclosed in the present invention can simultaneously purify multiple indoor air pollutants. Since the liquid-based purification method is adopted, and the water body itself can treat a variety of pollutant components in the air, by adjusting the composition of the purification liquid reasonably, the formaldehyde, nicotine and other volatile organic compounds in the air can be better absorbed to purify
  • the chemical composition in the liquid also allows it to kill microorganisms, viruses and bacteria in the indoor air. PM2.5 suspended particles can be easily adsorbed by the purification liquid and removed. If necessary, adding an appropriate amount of air cleaning agent can also better remove the air odor.
  • the nozzles 1-3 of the mixer 1 can be porous type. Nozzles 1-3a, the purification liquid in the purification liquid storage tank 3 should contain toluene absorbents, oil fume absorbents, such as formaldehyde absorbents such as chlorine dioxide, hydrogen peroxide, and fatty alcohol polyoxyethylene ether, sodium alkylbenzene sulfonate, The concentration of oil fume absorbents such as ethanol is about 1.5% to 5%, and the rest is water. After the entire device was running for 0.5 hours, the indoor air quality was significantly improved, and the content of dust, oil fume, and formaldehyde was well controlled. The indoor noise during the entire operation was very small, and the expected purification effect was achieved.
  • the nozzles 1-3 of the mixer 1 can be selected as orifice nozzles 1.
  • the purification liquid in the purification liquid storage tank 3 uses pure water (nicotine is easily soluble in water), and an appropriate amount of air freshener is added. After running for 2 hours, the nicotine content in the indoor air decreased rapidly, and the indoor noise was very small during the whole operation process, and a good air purification effect was achieved.

Abstract

A mixer (1) and a separated air purification device. The mixer (1) is used for mixing air and a purification liquid to generate a gas-liquid mixture. The air purification device comprises the mixer (1), a purification liquid storage tank (3) and an air suction inlet (5). A purification liquid inlet of the mixer (1) is in fluid communication with a purification liquid outlet (3-6) of the purification liquid storage tank (3) by means of a pump (2), an air inlet of the mixer (1) is in fluid communication with the air suction inlet (5), a diffusion pipe (1-6) of the mixer (1) is in fluid communication with a gas-liquid mixture inlet (3-2) on the purification liquid storage tank (3) by means of a pipeline (7), and a check valve (4) for preventing flow from reversing is arranged on the pipeline (7). The gas-liquid mixture leaving the mixer (1) enters the purification liquid storage tank (3) to complete gas-liquid separation, purified air returns to air from an air outlet (3-5) on a tank body, and the purification liquid re-enters the mixer (1) from the purification liquid outlet (3-6) to achieve cyclic utilization of the purification liquid.

Description

混合器及包含该混合器的分离式空气净化装置Mixer and separation type air purification device containing the mixer 技术领域Technical field
本发明公开至少一个实施例涉及一种混合器及包含该混合器的分离式空气净化装置。At least one embodiment disclosed in the present invention relates to a mixer and a separate air purification device including the mixer.
背景技术Background technique
近年来,随着我国经济水平的快速进步,人民的生活水平不断提高。与此同时,工业化的快速发展,也带来了严重的空气污染问题,影响了人们的身体健康。随着生产和生活方式的更加现代化,更多的工作和文娱体育活动都可在室内进行,人们的室内活动时间在逐渐提高。尤其是老、幼、病、残等体弱群体,户外活动机会更少,在室内度过的时间甚至高达93%以上,这就使得室内空气的污染问题尤其突出。据统计,室内环境污染已经引起35.7%的呼吸道疾病,22%的慢性肺病和15%的气管炎、支气管炎和肺癌。现代生活中空调的广泛使用在给人们带来舒适的环境的同时,也使得室内、外空气的流通进一步被限制,污染问题也更为严峻。室内空气污染已经成为对公众健康危害最大的五种环境因素之一。In recent years, with the rapid progress of my country's economic level, the people's living standards have continued to improve. At the same time, the rapid development of industrialization has also brought serious air pollution problems, affecting people's health. With the modernization of production and lifestyle, more work and recreational and sports activities can be carried out indoors, and people's indoor activity time is gradually increasing. Especially vulnerable groups such as the elderly, young, sick, and disabled have fewer opportunities for outdoor activities, and even more than 93% of the time spent indoors, which makes the problem of indoor air pollution particularly prominent. According to statistics, indoor environmental pollution has caused 35.7% of respiratory diseases, 22% of chronic lung diseases and 15% of bronchitis, bronchitis and lung cancer. The widespread use of air conditioners in modern life not only brings people a comfortable environment, but also makes the circulation of indoor and outdoor air further restricted, and the pollution problem is also more serious. Indoor air pollution has become one of the five environmental factors most harmful to public health.
室内环境污染物的主要成分有以下四大类:PM2.5悬浮颗粒物、甲醛尼古丁及其它挥发性有机物、微生物及病毒细菌和空气异味。The main components of indoor environmental pollutants are divided into the following four categories: PM2.5 suspended particulate matter, formaldehyde, nicotine and other volatile organic compounds, microorganisms, viruses, bacteria, and air odors.
为了应对越来越严峻的室内空气污染问题,室内空气净化技术逐渐受到人们的重视。目前,常用的空气净化技术主要有:光等离子技术、负离子技术、光触媒技术、HEPA高效过滤技术、静电集尘技术和活性氧技术等。在这些技术中,核心部件大多采用滤网或类似形式,虽然便于更换,但是也存在着比较多的问题:(1)空气与滤网的接触经常不够充分,直接影响了过滤效果;(2)净化空气的速度较慢,无法快速地对室内空气进行净化处理;(3)普适性较差,仅能针对某类空气污染物进行处理;(4)部分技术噪声大。In order to cope with the increasingly severe problem of indoor air pollution, indoor air purification technology has gradually attracted people's attention. At present, the commonly used air purification technologies mainly include: light plasma technology, negative ion technology, photocatalyst technology, HEPA high-efficiency filtration technology, electrostatic dust collection technology and active oxygen technology. In these technologies, most of the core components adopt filter screens or similar forms. Although it is easy to replace, there are many problems: (1) The contact between the air and the filter screen is often insufficient, which directly affects the filtering effect; (2) The air purification speed is slow, and the indoor air cannot be purified quickly; (3) The universality is poor, and it can only deal with certain types of air pollutants; (4) Some technologies are noisy.
发明内容Summary of the invention
本发明公开的至少一个实施例提供一种混合器及包含该混合器的分离式空气净化装置。在保证节能环保经济的同时,使室内空气得到更好的净化效果。At least one embodiment disclosed in the present invention provides a mixer and a separate air purification device including the mixer. While ensuring energy saving, environmental protection and economy, the indoor air can be purified better.
本发明公开的至少一个实施例提供一种混合器,包括:第一流体入口;第二流体入口;吸入室;将从第一流体入口和第二流体入口流入的两种流体混合的混合管;和使混合流体离开混合器的扩散管;所述第一流体入口通过喷嘴与所述吸入室流体连通,所述第二流体入口与所述吸入室流体连通,所述吸入室、所述混合管和所述扩散管依次流体连通,所述吸入室的流道面积沿着流体流动方向逐渐减小,所述混合管中靠近所述吸入室的部分为直管,所述混合管中远离所述吸入室的部分为波浪状的管道,所述扩散管的流道面积沿着流体流动方向逐渐增大。At least one embodiment disclosed in the present invention provides a mixer, including: a first fluid inlet; a second fluid inlet; a suction chamber; a mixing pipe that mixes two fluids flowing in from the first fluid inlet and the second fluid inlet; And a diffuser that allows the mixed fluid to leave the mixer; the first fluid inlet is in fluid communication with the suction chamber through a nozzle, the second fluid inlet is in fluid communication with the suction chamber, the suction chamber, the mixing pipe In fluid communication with the diffuser tube in sequence, the flow channel area of the suction chamber gradually decreases along the fluid flow direction, the part of the mixing tube close to the suction chamber is a straight tube, and the mixing tube is far away from the The part of the suction chamber is a wavy pipe, and the flow channel area of the diffuser pipe gradually increases along the fluid flow direction.
在一些示例中,所述吸入室中安装有多片弯曲的导流片,所述导流片从所述吸入室一端向另一端延伸。In some examples, a plurality of curved guide vanes are installed in the suction chamber, and the guide vanes extend from one end to the other end of the suction chamber.
在一些示例中,所述喷嘴为多孔型喷嘴。In some examples, the nozzle is a porous nozzle.
在一些示例中,所述喷嘴为呈倒锥形以增强流体的扩散角度的孔口型喷嘴。In some examples, the nozzle is an orifice nozzle having an inverted cone shape to enhance the diffusion angle of the fluid.
在一些示例中,所述吸入室内导流片的厚度在0.05D~0.1D之间,高度在0.1D~0.2D之间,其中D为所述混合管的直径。In some examples, the thickness of the deflector in the suction chamber is between 0.05D and 0.1D, and the height is between 0.1D and 0.2D, where D is the diameter of the mixing tube.
在一些示例中,所述混合管中所述直管长度为3D~5D,所述波浪状的管道长度介于12D~20D,其中D为所述混合管的直径。In some examples, the length of the straight pipe in the mixing pipe is 3D to 5D, and the length of the wave-shaped pipe is between 12D and 20D, where D is the diameter of the mixing pipe.
在一些示例中,所述扩散管的扩散角度β在8~12°之间。In some examples, the diffusion angle β of the diffusion tube is between 8 and 12°.
本发明公开的至少一个实施例提供一种分离式室内空气净化装置,包括所述的混合器、循环水泵、净化液存储箱和空气吸入口,所述净化液存储箱包括箱体以及位于所述箱体上的气液混合物入口、空气出口和净化液出口,所述混合器的所述第一流体入口通过所述循环水泵与所述净化液存储箱的所述净化液出口流体连通,所述混合器的所述第二流体入口与所述空气吸入口流体连通,所述混合器的所述扩散管通过管道与所述净化液存储箱上的所述气液混合物入口流体连通,所述管道上设有防止流动倒转的止回阀。At least one embodiment disclosed in the present invention provides a separate indoor air purification device, including the mixer, a circulating water pump, a purified liquid storage tank, and an air suction port. The gas-liquid mixture inlet, the air outlet and the purified liquid outlet on the tank, the first fluid inlet of the mixer is in fluid communication with the purified liquid outlet of the purified liquid storage tank through the circulating water pump, the The second fluid inlet of the mixer is in fluid communication with the air suction inlet, and the diffusion tube of the mixer is in fluid communication with the gas-liquid mixture inlet on the purification liquid storage tank through a pipe, and the pipe There is a check valve to prevent flow reversal.
在一些示例中,所述净化液存储箱的所述箱体内具有过滤掉经所述气液混合物入口流入的气液混合物中的固体颗粒的过滤室,和储存过滤后的净化液的储液室,其中所述气液混合物入口与所述过滤室流体连通,所述净化液出口与所述储液室流体连通,所述空气出口位于所述储液室和/或 所述过滤室上方。In some examples, the tank body of the purified liquid storage tank has a filter chamber that filters out solid particles in the gas-liquid mixture flowing in through the gas-liquid mixture inlet, and a liquid storage chamber that stores the filtered purified liquid , Wherein the gas-liquid mixture inlet is in fluid communication with the filter chamber, the purified liquid outlet is in fluid communication with the liquid storage chamber, and the air outlet is located above the liquid storage chamber and/or the filter chamber.
在一些示例中,所述净化液存储箱上的空气出口和/或空气吸入口设有隔离网。In some examples, the air outlet and/or the air suction inlet on the purified liquid storage tank are provided with isolation nets.
附图说明Description of the drawings
为了更清楚地说明本发明公开实施例的技术方案,下面将对实施例的附图作简单地介绍。In order to more clearly illustrate the technical solutions of the disclosed embodiments of the present invention, the accompanying drawings of the embodiments will be briefly introduced below.
图1为本发明公开一实施例提供的混合器剖面结构示意图。Fig. 1 is a schematic cross-sectional structure diagram of a mixer provided by an embodiment of the present disclosure.
图2为本发明公开另一实施例提供的混合器剖面结构示意图。2 is a schematic cross-sectional structure diagram of a mixer provided by another embodiment of the present disclosure.
图3a为本发明公开一实施例提供的带旋转导流片的吸入室结构示意图。Fig. 3a is a schematic structural diagram of a suction chamber with a rotating baffle provided by an embodiment of the present disclosure.
图3b为图3a所示的吸入室局部结构示意图。Fig. 3b is a schematic diagram of a partial structure of the suction chamber shown in Fig. 3a.
图4a为本发明公开一实施例提供的多孔型喷嘴正视图。Fig. 4a is a front view of a porous nozzle provided by an embodiment of the present disclosure.
图4b为本发明公开一实施例提供的多孔型喷嘴剖面示意图。4b is a schematic cross-sectional view of a porous nozzle provided by an embodiment of the present disclosure.
图5a为本发明公开一实施例提供的孔口型喷嘴正视图。Fig. 5a is a front view of an orifice nozzle provided by an embodiment of the present disclosure.
图5b为本发明公开一实施例提供的孔口型喷嘴剖面示意图。Figure 5b is a schematic cross-sectional view of an orifice nozzle provided by an embodiment of the present disclosure.
图6为本发明公开一实施例提供的分离式空气净化装置原理示意图。Fig. 6 is a schematic diagram of the principle of a separation air purification device provided by an embodiment of the present disclosure.
图7为本发明公开一实施例提供的净化液存储箱结构示意图。FIG. 7 is a schematic diagram of the structure of a purification liquid storage tank provided by an embodiment of the present disclosure.
附图标记说明:Description of reference signs:
1-混合器;1- Mixer;
2-循环水泵;2-Circulating water pump;
3-净化液存储箱;3- Purification liquid storage tank;
4-止回阀;4- check valve;
5-空气吸入口;5-Air suction port;
6-隔离网;6-Isolation network;
7-管道;7-pipe;
1-1-第一流体入口;1-1-The first fluid inlet;
1-2-第二流体入口;1-2-The second fluid inlet;
1-3-喷嘴;1-3-Nozzle;
1-3a-多孔型喷嘴;1-3a-Porous nozzle;
1-3b-孔口型喷嘴;1-3b-Orifice nozzle;
1-4-吸入室;1-4-Suction chamber;
1-5-混合管;1-5-mixing tube;
1-6-扩散管;1-6-diffusion tube;
3-1-净化液;3-1-Cleaning liquid;
3-2-气液混合物入口;3-2-gas-liquid mixture inlet;
3-3-隔离板;3-3-Isolation board;
3-4过滤网;3-4 filter screen;
3-6净化液出口;3-6 Purified liquid outlet;
3-7-废物排出口;3-7-Waste discharge outlet;
3-8-净化液原液补给装置;3-8- Purification liquid original liquid supply device;
3-9-水补给口。3-9-Water supply port.
具体实施方式Detailed ways
将描述一种混合器,术语“混合器”在本文中指的是混合流体的混合器。这样的混合器可混合空气和净化液产生净化空气流用于环境或气候的控制。优化了混合器结构,混合器内部会产生非常强烈的流体剪切混合作用,被吸入的空气与净化液充分混合与化学反应后会形成均匀的、含大量微小气泡的气液混合物,空气与净化液的接触混合十分充分,可最大化地发挥净化液的空气净化作用。A type of mixer will be described, and the term "mixer" herein refers to a mixer that mixes fluids. Such a mixer can mix air and purified liquid to produce a stream of purified air for environment or climate control. The structure of the mixer is optimized. The inside of the mixer will produce a very strong fluid shear mixing effect. The inhaled air and the purified liquid will be fully mixed and chemically reacted to form a uniform gas-liquid mixture containing a large number of tiny bubbles. The air and the purification The contact mixing of the liquid is very sufficient, which can maximize the air purification effect of the purification liquid.
图1为本发明公开一实施例提供的混合器剖面结构示意图;图2为本发明公开另一实施例提供的混合器剖面结构示意图。如图1和图2,混合器包括第一流体入口1-1,第二流体入口1-2,吸入室1-4,将从第一流体入口1-1和第二流体入口1-2流入的两种流体混合的混合管1-5,和使混合流体离开混合器的扩散管1-6。第一流体入口1-1通过喷嘴1-3与吸入室1-4流体连通,喷嘴1-3伸入吸入室1-4内,第二流体入口1-2与吸入室1-4流体连通,吸入室1-4、混合管1-5和扩散管1-6依次流体连通。吸入室1-4的管径沿着流体流动方向逐渐减小,扩散管1-6的管径沿着流体流动方向逐渐减大。为了提高混合器的混合效果,混合管1-5中靠近吸入室1-4的部分为直管,混合管1-5中远离吸入室1-4的部分为波浪状的管道。Fig. 1 is a schematic cross-sectional structure diagram of a mixer provided by an embodiment of the present disclosure; Fig. 2 is a schematic cross-sectional structure diagram of a mixer provided by another embodiment of the present disclosure. As shown in Figures 1 and 2, the mixer includes a first fluid inlet 1-1, a second fluid inlet 1-2, and a suction chamber 1-4, which will flow from the first fluid inlet 1-1 and the second fluid inlet 1-2 The mixing pipe 1-5 for mixing the two fluids, and the diffuser pipe 1-6 for the mixed fluid to leave the mixer. The first fluid inlet 1-1 is in fluid communication with the suction chamber 1-4 through the nozzle 1-3, the nozzle 1-3 extends into the suction chamber 1-4, and the second fluid inlet 1-2 is in fluid communication with the suction chamber 1-4, The suction chamber 1-4, the mixing pipe 1-5 and the diffusion pipe 1-6 are in fluid communication in sequence. The pipe diameter of the suction chamber 1-4 gradually decreases along the fluid flow direction, and the pipe diameter of the diffuser pipe 1-6 gradually decreases along the fluid flow direction. In order to improve the mixing effect of the mixer, the part of the mixing pipe 1-5 close to the suction chamber 1-4 is a straight pipe, and the part of the mixing pipe 1-5 far from the suction chamber 1-4 is a wavy pipe.
用混合器混合空气和净化液产生净化空气流时,第一流体入口1-1处 流体为经过加压后压力较高的净化液流体,第二流体入口1-2处的为压力较低的待净化空气,净化液经第一流体入口1-1、喷嘴1-3进入吸入室1-4后,流道面积减小,形成多股高速流体,进入混合管1-5,由于高速流体的卷吸作用,会在混合管1-5处形成低压区,在该处低压与外界大气压的压差作用下,待净化空气被吸入混合器1内部,在混合管1-5内与净化液混合,气液混合物经过扩散管1-6离开混合器。When a mixer is used to mix air and purifying liquid to produce a purified air stream, the fluid at the first fluid inlet 1-1 is the purified fluid with higher pressure after being pressurized, and the fluid at the second fluid inlet 1-2 is the lower pressure For the air to be purified, after the purified liquid enters the suction chamber 1-4 through the first fluid inlet 1-1 and nozzles 1-3, the flow channel area is reduced, forming multiple high-speed fluids, which enter the mixing pipe 1-5. Entrainment will form a low pressure zone at the mixing pipe 1-5. Under the effect of the pressure difference between the low pressure and the outside atmospheric pressure, the air to be purified is sucked into the mixer 1 and mixed with the purified liquid in the mixing pipe 1-5 , The gas-liquid mixture leaves the mixer through the diffuser 1-6.
空气和净化液在混合管1-5内会充分混合,形成均匀的、含有大量微小气泡的气液混合物,使得空气与净化液充分混合与反应,在净化液的作用下,可达到很好的空气净化效果。又由于混合器对空气的抽吸能力很强,故而能在短时间内对大量被污染的空气进行处理。另外,采用基于液体的净化液处理空气,能够同时对多类污染物进行处理,普适性较强,适用范围广。The air and the purification liquid will be fully mixed in the mixing tube 1-5 to form a uniform gas-liquid mixture containing a large number of tiny bubbles, so that the air and the purification liquid can be fully mixed and reacted. Under the action of the purification liquid, a good Air purification effect. And because the mixer has a strong suction capacity for air, it can treat a large amount of contaminated air in a short time. In addition, the use of liquid-based purification fluids to treat air can simultaneously treat multiple types of pollutants, with strong universality and wide application scope.
如图3a、图3b,为了提高混合器的混合效果,吸入室1-4中安装了多片弯曲的导流片,所述导流片从吸入室1-4一端向另一端延伸。As shown in Fig. 3a and Fig. 3b, in order to improve the mixing effect of the mixer, a plurality of curved guide vanes are installed in the suction chamber 1-4, and the guide vanes extend from one end to the other end of the suction chamber 1-4.
参考图1、图4a和图4b,喷嘴1-3可为多孔型喷嘴1-3a,多孔型喷嘴1-3a布置有多个孔结构,会使得净化液由单股转化为多股高速流体,增加了与空气的接触面积,进而显著增强了其抽吸空气的能力,适用于对空气净化速度要求较高的场合。Referring to Figure 1, Figure 4a and Figure 4b, the nozzles 1-3 can be porous nozzles 1-3a. The porous nozzles 1-3a are arranged with multiple pore structures, which will transform the purification liquid from a single strand to multiple high-speed fluids. The contact area with the air is increased, thereby significantly enhancing its ability to suck air, and is suitable for occasions that require high air purification speed.
参考图2、图5a和图5b,喷嘴1-3还可为孔口型喷嘴1-3b,孔口型喷嘴1-3b呈倒锥形,可大大增强流经该部件流体的扩散角度,虽然其混合效果与多孔型喷嘴1-3a相比稍弱,但是其流动损失更小,适用于对节能更加注重的场合。Referring to Figure 2, Figure 5a and Figure 5b, nozzles 1-3 can also be orifice nozzles 1-3b, orifice nozzles 1-3b are inverted cones, which can greatly enhance the diffusion angle of the fluid flowing through the component, although Its mixing effect is slightly weaker than the porous nozzle 1-3a, but its flow loss is smaller, which is suitable for occasions where energy saving is more important.
为了近一步增强混合器对空气的抽吸能力及混合作用,加快空气净化速度,对混合器主要结构参数范围进行界定。为了便于表述,将混合器混合管1-5的直径D作为基准量。混合器主要结构参数可以为:第一流体入口1-1内径约为1.2D~1.5D;第二流体入口1-2内径约为2D~4D;喷嘴1-3距离混合管1-5入口的距离约为0.7D~1.5D,直径约为0.3D~0.6D;多孔型喷嘴1-3a厚度约为2.5mm~5mm,孔数量为4~12个,各个孔的大小可以不一致,根据实际需要进行调整;孔口型喷嘴1-3b孔口直径约为0.15D~0.45D,厚度约为2.5mm~5mm,角度为30°~45°;吸入室1-4 的收缩角度α在60°~120°之间,导流片的厚度为0.05D~0.1D,高度约为0.1D~0.2D;混合管1-5的长度L与直径D的比值L/D应在15~25之间,混合管1-5直管段长度约为3D~5D,波浪状的管道长度介于12D~20D;扩散管1-6的扩散角度β在8~12°之间,长度介于5D~9D。In order to further enhance the air suction capacity and mixing effect of the mixer, and accelerate the air purification speed, the range of the main structural parameters of the mixer is defined. For ease of description, the diameter D of the mixer mixing tube 1-5 is taken as the reference quantity. The main structural parameters of the mixer can be: the inner diameter of the first fluid inlet 1-1 is about 1.2D~1.5D; the inner diameter of the second fluid inlet 1-2 is about 2D~4D; the distance between the nozzle 1-3 and the inlet of the mixing tube 1-5 The distance is about 0.7D~1.5D, the diameter is about 0.3D~0.6D; the thickness of the porous nozzle 1-3a is about 2.5mm~5mm, the number of holes is 4~12, the size of each hole can be different, according to actual needs Adjust; the orifice diameter of the orifice nozzle 1-3b is about 0.15D~0.45D, the thickness is about 2.5mm~5mm, and the angle is 30°~45°; the contraction angle α of the suction chamber 1-4 is 60°~ Between 120°, the thickness of the deflector is 0.05D~0.1D, and the height is about 0.1D~0.2D; the ratio L/D of the length L to the diameter D of the mixing tube 1-5 should be between 15-25, The length of the straight pipe section of the mixing pipe 1-5 is about 3D~5D, and the length of the wavy pipe is between 12D~20D; the diffusion angle β of the diffuser pipe 1-6 is between 8~12°, and the length is between 5D~9D.
图6为本发明公开一实施例提供的分离式空气净化装置原理示意图。如图6,分离式空气净化装置包括上文所述的混合器1、循环水泵2、净化液存储箱3和空气吸入口5。Fig. 6 is a schematic diagram of the principle of a separation air purification device provided by an embodiment of the present disclosure. As shown in Fig. 6, the separation type air purification device includes the mixer 1, the circulating water pump 2, the purified liquid storage tank 3 and the air suction port 5 as described above.
其中循环水泵2为整个净化装置提供循环动力,其内部与液体接触表面均经过特殊处理(如采用PVC材质制造泵体、泵表面喷涂抗腐蚀涂层等),以提高其抗腐蚀性,且其工作噪音很小。空气吸入口5为一末端呈喇叭状的管道,置于待净化的环境中,并通过管道与混合器1相连,主要功能为将待净化空气导入混合器1内部。此外,空气吸入口5还可设置隔离网6,避免部分重量较轻的杂物被吸进混合器。Among them, the circulating water pump 2 provides circulating power for the entire purification device, and its internal liquid contact surface has been specially treated (such as the use of PVC material to make the pump body, the pump surface is sprayed with anti-corrosion coating, etc.) to improve its corrosion resistance, and its Working noise is very small. The air suction port 5 is a pipe with a horn-shaped end, which is placed in the environment to be purified and connected to the mixer 1 through the pipe. The main function is to introduce the air to be purified into the mixer 1. In addition, the air suction port 5 can also be provided with an isolation net 6 to prevent some lighter sundries from being sucked into the mixer.
图7为本发明公开一实施例提供的净化液存储箱结构示意图。如图7,净化液存储箱3包括箱体,以及位于箱体上的气液混合物入口3-2、空气出口3-5和净化液出口3-6。所述箱体内装有预先调制好的净化液3-1,其主要成分可以根据室内空气污染物的具体情况灵活更改,以达到最佳的净化效果。所述箱体顶部开口可以作为空气出口3-5。FIG. 7 is a schematic diagram of the structure of a purification liquid storage tank provided by an embodiment of the present disclosure. As shown in Fig. 7, the purified liquid storage tank 3 includes a tank body, and a gas-liquid mixture inlet 3-2, an air outlet 3-5 and a purified liquid outlet 3-6 located on the tank body. The pre-prepared purification liquid 3-1 is installed in the tank, and its main components can be flexibly changed according to the specific conditions of indoor air pollutants to achieve the best purification effect. The opening at the top of the box can be used as an air outlet 3-5.
此外,可在净化液存储箱3的所述箱体内设置过滤室和储液室,所述过滤室用于过滤掉从混合器1离开的气液混合物中的固体颗粒,过滤后的净化液进入到储液室。因此,所述过滤室与气液混合物入口3-2流体连通,所述储液室与空气出口3-5和净化液出口3-6流体连通。在一种可能的实施方式中,所述过滤室和所述储液室可由所述箱体的内壁、隔离板3-3和过滤网3-4围成。隔离板3-3竖直设置在所述箱体内。过滤网3-4横向设置,一侧边与隔离板3-3连接,另外三个侧边与所述箱体内壁连接。过滤网3-4可以是可拆卸式的,便于清洗。In addition, a filter chamber and a liquid storage chamber can be provided in the tank body of the purified liquid storage tank 3. The filter chamber is used to filter out solid particles in the gas-liquid mixture leaving the mixer 1, and the filtered purified liquid enters To the reservoir. Therefore, the filter chamber is in fluid communication with the gas-liquid mixture inlet 3-2, and the liquid storage chamber is in fluid communication with the air outlet 3-5 and the purified liquid outlet 3-6. In a possible implementation, the filter chamber and the liquid storage chamber may be enclosed by the inner wall of the box body, the isolation plate 3-3, and the filter mesh 3-4. The isolation board 3-3 is vertically arranged in the box. The filter screen 3-4 is arranged horizontally, one side is connected with the isolation plate 3-3, and the other three sides are connected with the inner wall of the box. The filter 3-4 can be detachable for easy cleaning.
此外,在净化液存储箱3上还可设置废物排出口3-7、净化液原液补给装置3-8及水补给口3-9。废物排出口3-7与所述过滤室流体连通,由过滤网3-4过滤下来的固体颗粒及废液可在设备不工作时由废物排出口3-7排出。净化液原液补给装置3-8可以通过现有技术实时监测净化液中 各种净化有效成分的含量,并及时补充净化液原液,保证整个净化装置中净化液3-1的质量。通过水补给口3-9可以向净化液存储箱3内补充适量的水分,以补偿整个装置运行过程中水分的消耗。In addition, a waste discharge port 3-7, a purification liquid stock replenishment device 3-8, and a water replenishment port 3-9 can also be provided on the purified liquid storage tank 3. The waste outlet 3-7 is in fluid communication with the filter chamber, and the solid particles and waste liquid filtered by the filter mesh 3-4 can be discharged from the waste outlet 3-7 when the equipment is not working. The purifying liquid stock replenishing device 3-8 can monitor the content of various purification active ingredients in the purified liquid in real time through the existing technology, and timely replenish the purified liquid stock to ensure the quality of the purified liquid 3-1 in the entire purification device. An appropriate amount of water can be added to the purified liquid storage tank 3 through the water supply port 3-9 to compensate for the water consumption during the operation of the entire device.
继续参考图6,混合器1的第一流体入口1-1通过循环水泵2与净化液存储箱3的净化液出口3-6流体连通,混合器1的第二流体入口1-2与空气吸入口5流体连通,混合器1的扩散管1-6与净化液存储箱3上的气液混合物入口3-2流体连通,扩散管1-6与气液混合物入口3-2之间的管道7上设有防止流动倒转的止回阀4。Continuing to refer to Figure 6, the first fluid inlet 1-1 of the mixer 1 is in fluid communication with the purified fluid outlet 3-6 of the purified fluid storage tank 3 through the circulating water pump 2, and the second fluid inlet 1-2 of the mixer 1 is inhaled with air. Port 5 is in fluid communication, the diffuser tube 1-6 of the mixer 1 is in fluid communication with the gas-liquid mixture inlet 3-2 on the purification liquid storage tank 3, and the pipe 7 between the diffuser tube 1-6 and the gas-liquid mixture inlet 3-2 There is a check valve 4 to prevent flow reversal.
离开混合器1的气液混合物通过净化液存储箱3上的气液混合物入口3-2进入所述箱体内部的所述过滤室后会经过滤网3-4,一方面可以将混合物中可能存在的固体过滤,另一方面进一步促进了空气与净化液的接触,可以提高净化效果。气液混合物在所述箱体中完成气液分离,净化后的空气由空气出口3-5返回空气中,净化液则由隔离板3-3顶部进入净化液存储箱3另一侧的所述储液室,并由净化液出口3-6再次进入净化装置管道,实现净化液的循环利用。The gas-liquid mixture leaving the mixer 1 enters the filter chamber inside the tank through the gas-liquid mixture inlet 3-2 on the purified liquid storage tank 3, and then passes through the filter screen 3-4. The existing solid filtration, on the other hand, further promotes the contact between the air and the purification liquid, which can improve the purification effect. The gas-liquid mixture completes the gas-liquid separation in the tank, the purified air returns to the air through the air outlet 3-5, and the purified liquid enters the other side of the purified liquid storage tank 3 from the top of the isolation plate 3-3. The liquid storage chamber enters the purification device pipeline from the purification liquid outlet 3-6 again to realize the recycling of the purification liquid.
值得注意的是,经混合后逸出的体气携带大量的水珠,若直接排出,室内空气湿度将增大,为了对气体进行脱水,可在空气出口3-5设置多孔结构的隔离网。It is worth noting that the body gas that escapes after mixing carries a large amount of water droplets. If it is directly discharged, the indoor air humidity will increase. In order to dehydrate the gas, a porous structure isolation net can be set at the air outlet 3-5.
需要注意的是,可以做大型的混合器1以加快空气净化速率,但这样混合器1内部会发生剧烈的空气、净化液混合,产生较强的噪音,为了避免产生室内噪音污染,故将混合器1单独至于室外,空气净化装置的其余部件在室内,各部件通过管道连接。如果混合器1小型化,也是可以置于室内的。It should be noted that a large-scale mixer 1 can be made to speed up the air purification rate, but in this way, violent air and purification liquid mixing will occur inside the mixer 1, resulting in strong noise. In order to avoid indoor noise pollution, the mixing The device 1 is alone outdoors, the remaining parts of the air purification device are indoors, and the parts are connected by pipes. If the mixer 1 is miniaturized, it can also be placed indoors.
本发明公开的混合器1结构简单、易于制造、运行可靠,空气净化装置其它部件也比较便宜,因而整个净化装置经济实惠,运行可靠,便于推广。The mixer 1 disclosed in the present invention is simple in structure, easy to manufacture, and reliable in operation, and other parts of the air purification device are relatively cheap, so the entire purification device is economical, reliable in operation, and easy to popularize.
本发明公开所述的空气净化装置可以同时对多种室内空气污染物进行净化。由于采用基于液体的净化方式,而且水体本身就能对空气中的多种污染成分进行处理,那么通过合理调整净化液的组成,可以更好地吸收空气中的甲醛尼古丁及其它挥发性有机物,净化液中的化学成分也使得其 可以很好地杀死室内空气中的微生物及病毒细菌,PM2.5悬浮颗粒物则可以很轻易地被净化液吸附而被去除。如有需要在其中加入适量的空气清洗剂也可以较好地去除空气异味。The air purification device disclosed in the present invention can simultaneously purify multiple indoor air pollutants. Since the liquid-based purification method is adopted, and the water body itself can treat a variety of pollutant components in the air, by adjusting the composition of the purification liquid reasonably, the formaldehyde, nicotine and other volatile organic compounds in the air can be better absorbed to purify The chemical composition in the liquid also allows it to kill microorganisms, viruses and bacteria in the indoor air. PM2.5 suspended particles can be easily adsorbed by the purification liquid and removed. If necessary, adding an appropriate amount of air cleaning agent can also better remove the air odor.
使用本发明公开所述的空气净化装置对污染较为严重、污染成分主要为悬浮灰尘、家具释放的甲苯、烹调产生的油烟的室内空气进行净化时,混合器1的喷嘴1-3可选用多孔型喷嘴1-3a,净化液存储箱3内的净化液中应包含甲苯吸收剂、油烟吸收剂,如二氧化氯、双氧水等甲醛吸收剂和脂肪醇聚氧乙烯醚、烷基苯磺酸钠、乙醇等油烟吸收剂,其浓度约为1.5%~5%,其余部分为水。整个装置运行0.5小时后,室内空气质量明显提高,灰尘、油烟、甲醛含量得到较好的控制,整个运行过程中室内噪音很小,取得了预期的净化效果。When the air purification device disclosed in the present invention is used to purify the indoor air with serious pollution, suspended dust, toluene released from furniture, and cooking fumes, the nozzles 1-3 of the mixer 1 can be porous type. Nozzles 1-3a, the purification liquid in the purification liquid storage tank 3 should contain toluene absorbents, oil fume absorbents, such as formaldehyde absorbents such as chlorine dioxide, hydrogen peroxide, and fatty alcohol polyoxyethylene ether, sodium alkylbenzene sulfonate, The concentration of oil fume absorbents such as ethanol is about 1.5% to 5%, and the rest is water. After the entire device was running for 0.5 hours, the indoor air quality was significantly improved, and the content of dust, oil fume, and formaldehyde was well controlled. The indoor noise during the entire operation was very small, and the expected purification effect was achieved.
使用本发明公开所述的空气净化装置对污染较轻、主要污染物为吸烟产生的尼古丁,且存在一定异味的室内环境进行净化时,混合器1的喷嘴1-3可选用孔口型喷嘴1-3b,净化液存储箱3内的净化液使用纯水(尼古丁易溶于水),并加入适量的空气清新剂。运行2小时后,室内空气中尼古丁含量迅速降低,整个运行过程中室内噪音很小,取得了很好的空气净化效果。When the air purification device disclosed in the present invention is used to purify an indoor environment with relatively light pollution, the main pollutant being nicotine produced by smoking, and a certain peculiar smell, the nozzles 1-3 of the mixer 1 can be selected as orifice nozzles 1. -3b, the purification liquid in the purification liquid storage tank 3 uses pure water (nicotine is easily soluble in water), and an appropriate amount of air freshener is added. After running for 2 hours, the nicotine content in the indoor air decreased rapidly, and the indoor noise was very small during the whole operation process, and a good air purification effect was achieved.

Claims (10)

  1. 一种混合器(1),其特征在于,包括:第一流体入口(1-1);第二流体入口(1-2);吸入室(1-4);将从第一流体入口(1-1)和第二流体入口(1-2)流入的两种流体混合的混合管(1-5);和使混合流体离开混合器的扩散管(1-6);第一流体入口(1-1)通过喷嘴(1-3)与吸入室(1-4)流体连通,第二流体入口(1-2)与吸入室(1-4)流体连通,吸入室(1-4)、混合管(1-5)和扩散管(1-6)依次流体连通,吸入室(1-4)的流道面积沿着流体流动方向逐渐减小,混合管(1-5)中靠近吸入室(1-4)的部分为直管,混合管(1-5)中远离吸入室(1-4)的部分为波浪状的管道,扩散管(1-6)的流道面积沿着流体流动方向逐渐增大。A mixer (1), characterized by comprising: a first fluid inlet (1-1); a second fluid inlet (1-2); a suction chamber (1-4); from the first fluid inlet (1) -1) Mixing pipe (1-5) that mixes the two fluids flowing in with the second fluid inlet (1-2); and the diffuser pipe (1-6) that allows the mixed fluid to leave the mixer; the first fluid inlet (1 -1) The nozzle (1-3) is in fluid communication with the suction chamber (1-4), the second fluid inlet (1-2) is in fluid communication with the suction chamber (1-4), and the suction chamber (1-4) is mixed The pipes (1-5) and the diffuser pipes (1-6) are in fluid communication in sequence, the flow channel area of the suction chamber (1-4) gradually decreases along the fluid flow direction, and the mixing pipe (1-5) is close to the suction chamber ( The part of 1-4) is a straight pipe, the part of the mixing pipe (1-5) far away from the suction chamber (1-4) is a wavy pipe, and the flow channel area of the diffuser (1-6) is along the fluid flow direction Gradually increase.
  2. 根据权利要求1所述的混合器,其特征在于,吸入室(1-4)中安装有多片弯曲的导流片,所述导流片从吸入室(1-4)一端向另一端延伸。The mixer according to claim 1, wherein a plurality of curved guide vanes are installed in the suction chamber (1-4), and the guide vanes extend from one end to the other end of the suction chamber (1-4) .
  3. 根据权利要求1所述的混合器,其特征在于,喷嘴(1-3)为多孔型喷嘴(1-3a)。The mixer according to claim 1, wherein the nozzle (1-3) is a porous nozzle (1-3a).
  4. 根据权利要求1所述的混合器,其特征在于,喷嘴(1-3)为呈倒锥形以增强流体的扩散角度的孔口型喷嘴(1-3b)。The mixer according to claim 1, wherein the nozzle (1-3) is an orifice nozzle (1-3b) with an inverted cone shape to enhance the diffusion angle of the fluid.
  5. 根据权利要求2所述的混合器,其特征在于,吸入室(1-4)内导流片的厚度在0.05D~0.1D之间,高度在0.1D~0.2D之间,其中D为混合管(1-5)的直径。The mixer according to claim 2, wherein the thickness of the deflector in the suction chamber (1-4) is between 0.05D and 0.1D, and the height is between 0.1D and 0.2D, where D is the mixing The diameter of the tube (1-5).
  6. 根据权利要求1所述的混合器,其特征在于,混合管(1-5)中所述直管长度为3D~5D,所述波浪状的管道长度介于12D~20D,其中D为混合管(1-5)的直径。The mixer according to claim 1, characterized in that the length of the straight pipe in the mixing pipe (1-5) is 3D~5D, the length of the wave-shaped pipe is between 12D~20D, where D is the mixing pipe (1-5) diameter.
  7. 根据权利要求1所述的混合器,其特征在于,扩散管(1-6)的扩散角度β在8~12°之间。The mixer according to claim 1, wherein the diffusion angle β of the diffusion tube (1-6) is between 8 and 12°.
  8. 一种分离式室内空气净化装置,其特征在于,包括权利要求1-7任一项所述的混合器(1)、循环水泵(2)、净化液存储箱(3)和空气吸入口(5),净化液存储箱(3)包括箱体以及位于所述箱体上的气液混合物入口(3-2)、空气出口(3-5)和净化液出口(3-6),混合器(1)的第一流体入口(1-1)通过循环水泵(2)与净化液存储箱(3)的净化液出口(3-6)流体连通,混合器(1)的第二流体入口(1-2)与空气吸入口(5)流体连通,混合器(1)的扩散管(1-6)通过管道(7)与净化液存储箱(3)上的气液混合物入口(3-2)流体连通,管道(7)上 设有防止流动倒转的止回阀(4)。A separate indoor air purification device, characterized by comprising the mixer (1) according to any one of claims 1-7, a circulating water pump (2), a purified liquid storage tank (3) and an air suction port (5) ), the purified liquid storage tank (3) includes a tank body and a gas-liquid mixture inlet (3-2), an air outlet (3-5) and a purified liquid outlet (3-6) on the tank body, and a mixer ( 1) The first fluid inlet (1-1) is in fluid communication with the purified liquid outlet (3-6) of the purified liquid storage tank (3) through the circulating water pump (2), and the second fluid inlet (1) of the mixer (1) -2) In fluid communication with the air suction port (5), the diffuser (1-6) of the mixer (1) is connected to the gas-liquid mixture inlet (3-2) on the purified liquid storage tank (3) through the pipe (7) The pipeline (7) is provided with a non-return valve (4) to prevent the flow from reversing.
  9. 根据权利要求8所述的分离式室内空气净化装置,其特征在于,净化液存储箱(3)的所述箱体内具有过滤掉经气液混合物入口(3-2)流入的气液混合物中的固体颗粒的过滤室,和储存过滤后的净化液的储液室,其中气液混合物入口(3-2)与所述过滤室流体连通,净化液出口(3-6)与所述储液室流体连通,空气出口(3-5)位于所述储液室和/或所述过滤室上方。The separated indoor air purification device according to claim 8, characterized in that the tank body of the purified liquid storage tank (3) is provided with filtering out of the gas-liquid mixture flowing in through the gas-liquid mixture inlet (3-2) A filter chamber for solid particles and a liquid storage chamber for storing filtered purified liquid, wherein the gas-liquid mixture inlet (3-2) is in fluid communication with the filter chamber, and the purified liquid outlet (3-6) is connected to the liquid storage chamber In fluid communication, the air outlet (3-5) is located above the liquid storage chamber and/or the filter chamber.
  10. 根据权利要求8所述的分离式室内空气净化装置,其特征在于,净化液存储箱(3)上的空气出口(3-5)和/或空气吸入口(5)设有隔离网。The separated indoor air purification device according to claim 8, characterized in that the air outlet (3-5) and/or the air suction inlet (5) on the purified liquid storage tank (3) is provided with an isolation net.
PCT/CN2020/121480 2020-04-30 2020-10-16 Mixer and separated air purification device comprising same WO2021218052A1 (en)

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Publication number Priority date Publication date Assignee Title
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Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4828768A (en) * 1983-06-10 1989-05-09 Chevron Research Company Jet scrubber and method of operation
CN202823113U (en) * 2012-09-28 2013-03-27 营口三征新科技化工有限公司 High-concentration acid-base tail gas treatment device
CN106731610A (en) * 2017-01-10 2017-05-31 兰州兰石重工有限公司 Venturi reactor type clarifying smoke system
CN107013242A (en) * 2017-05-23 2017-08-04 辽宁工程技术大学 A kind of mining multistage atomizing two-phase flow water mists generating means
CN107952316A (en) * 2016-10-17 2018-04-24 株式会社奥思伟 Micronic dust remover without strainer
CN108654549A (en) * 2018-06-14 2018-10-16 吴贵岚 A kind of venturi injection mixing reactor, a kind of oleamide are continuously synthesizing to device and its application method
CN111514702A (en) * 2020-04-30 2020-08-11 武汉大学 Mixer and separation type air purification device comprising same

Family Cites Families (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3622270A (en) * 1970-02-27 1971-11-23 Chemical Construction Corp Removal of sulfur dioxide from gas streams
CN201664585U (en) * 2010-03-12 2010-12-08 重庆欣欣向荣精细化工有限公司 Gas-liquid mixing ejector for ethyl vanillin oxidation tower
CN202490711U (en) * 2011-08-29 2012-10-17 太平洋水处理工程有限公司 Cyclone-type Venturi jet aeration nozzle
CN102500256A (en) * 2011-11-11 2012-06-20 南通申东冶金机械有限公司 Rotary jet mixer
CN108211751B (en) * 2017-05-02 2019-04-09 中国石油化工股份有限公司 The split type venturi washing sterilizer of spiral feed liquor
CN208599656U (en) * 2018-08-09 2019-03-15 天恒量子(厦门)科技集团有限公司 A kind of gas-fluid mixing systems device

Patent Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4828768A (en) * 1983-06-10 1989-05-09 Chevron Research Company Jet scrubber and method of operation
CN202823113U (en) * 2012-09-28 2013-03-27 营口三征新科技化工有限公司 High-concentration acid-base tail gas treatment device
CN107952316A (en) * 2016-10-17 2018-04-24 株式会社奥思伟 Micronic dust remover without strainer
CN106731610A (en) * 2017-01-10 2017-05-31 兰州兰石重工有限公司 Venturi reactor type clarifying smoke system
CN107013242A (en) * 2017-05-23 2017-08-04 辽宁工程技术大学 A kind of mining multistage atomizing two-phase flow water mists generating means
CN108654549A (en) * 2018-06-14 2018-10-16 吴贵岚 A kind of venturi injection mixing reactor, a kind of oleamide are continuously synthesizing to device and its application method
CN111514702A (en) * 2020-04-30 2020-08-11 武汉大学 Mixer and separation type air purification device comprising same

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