WO2017169897A1 - Air purification device - Google Patents

Air purification device Download PDF

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Publication number
WO2017169897A1
WO2017169897A1 PCT/JP2017/010894 JP2017010894W WO2017169897A1 WO 2017169897 A1 WO2017169897 A1 WO 2017169897A1 JP 2017010894 W JP2017010894 W JP 2017010894W WO 2017169897 A1 WO2017169897 A1 WO 2017169897A1
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WO
WIPO (PCT)
Prior art keywords
air
gas
liquid contact
water
cleaning water
Prior art date
Application number
PCT/JP2017/010894
Other languages
French (fr)
Japanese (ja)
Inventor
藤田 雅司
山中 弘次
Original Assignee
オルガノ株式会社
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Filing date
Publication date
Application filed by オルガノ株式会社 filed Critical オルガノ株式会社
Priority to CN201780018884.5A priority Critical patent/CN109069683A/en
Publication of WO2017169897A1 publication Critical patent/WO2017169897A1/en

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    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F24HEATING; RANGES; VENTILATING
    • F24FAIR-CONDITIONING; AIR-HUMIDIFICATION; VENTILATION; USE OF AIR CURRENTS FOR SCREENING
    • F24F7/00Ventilation
    • F24F7/003Ventilation in combination with air cleaning
    • 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
    • A61L9/16Disinfection, sterilisation or deodorisation of air using physical phenomena
    • 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
    • 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
    • B01D47/12Washers with plural different washing sections
    • 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
    • B01D47/14Packed scrubbers
    • 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
    • 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
    • B01D53/34Chemical or biological purification of waste gases
    • B01D53/38Removing components of undefined structure
    • 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
    • B01D53/34Chemical or biological purification of waste gases
    • B01D53/74General processes for purification of waste gases; Apparatus or devices specially adapted therefor
    • B01D53/77Liquid phase processes
    • B01D53/78Liquid phase processes with gas-liquid contact
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02ATECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
    • Y02A50/00TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE in human health protection, e.g. against extreme weather
    • Y02A50/20Air quality improvement or preservation, e.g. vehicle emission control or emission reduction by using catalytic converters
    • Y02A50/2351Atmospheric particulate matter [PM], e.g. carbon smoke microparticles, smog, aerosol particles, dust

Definitions

  • the present invention relates to an air purification device.
  • air purifiers that remove fine particles or gaseous substances contained in air by bringing cleaning water into contact with air have been used.
  • a gas-liquid contact type air purifier scrubbers used for building air conditioners and external air conditioners, and for dust removal and deodorization of exhaust gas in the manufacture of various products are known.
  • a filling scrubber using a filler such as Raschig ring, terralet packing, or a fiber assembly is known.
  • Filling scrubbers are roughly classified into two types: vertical (vertical) and horizontal (horizontal).
  • the vertical scrubber is a scrubber configured such that air flows vertically from below to the filler
  • the horizontal scrubber is configured such that air flows horizontally relative to the filler. It is.
  • Vertical scrubbers are widely used for industrial purposes, such as dust removal and deodorization of exhaust gas associated with the manufacture of various products.
  • the height of the packed bed is increased and the apparatus is enlarged, it is used for home use, that is, for purifying the outside air introduced into the living space and the air circulating in the living space in a house such as a detached house or an apartment house. It is not preferable.
  • the flow of cleaning water (downward) and the flow of air (upward) are countercurrent in the filler. For this reason, when the air flow rate is increased, there is a problem that flooding that eventually causes the washing water not to flow downward occurs, and gas-liquid contact is not sufficiently performed.
  • the flow of washing water (downward) and the flow of air (laterally) are vertical in the filler. Therefore, there is an advantage that the flows are less likely to interfere and the occurrence of flooding can be suppressed, and the present invention is suitably used for various applications.
  • a horizontal scrubber as a method of supplying cleaning water to the filler, a method of injecting cleaning water from a plurality of nozzles provided in front of the filler (upstream in the air flow direction) or above the filler, respectively. Is known (see, for example, Patent Documents 1 and 2).
  • An object of the present invention is to provide an air purification apparatus that removes particulates and gaseous substances contained in air with high efficiency while realizing downsizing of the apparatus.
  • an air purification device includes an intake port and an exhaust port provided in a housing such that air flows in a horizontal direction inside the housing, and an intake port and an exhaust port.
  • a gas-liquid contact part that is provided between the gas inlet and the air-liquid contact part for contacting the air introduced into the housing from the intake port with the cleaning water, and is provided upstream of the gas-liquid contact part with respect to the air flow direction.
  • Cleaning water jetting means for jetting cleaning water in a plane in a direction crossing the flow direction.
  • the air purification device of the present invention can be suitably used for household use, that is, for purifying the outside air introduced into the living space and the air circulating in the living space in a house such as a detached house or a housing complex.
  • it can also be suitably used for industrial use, for example, exhaust from food, pharmaceutical, chemical product manufacturing factories, pulp and paper factories, food and beverage kitchens, livestock barns, animal experiment facilities, It can be used as an application to treat (purify, remove dust, deodorize, etc.) odors from garbage storage sites and waste disposal sites.
  • FIG. 1 is a schematic diagram showing the configuration of the air purification device according to the first embodiment of the present invention.
  • the air purification device 1 is configured so that air flows in the horizontal direction inside the housing 2, and includes an intake port 3 and an exhaust port 4 provided on both sides of the housing 2 in the horizontal direction, and an intake port. 3 and a gas-liquid contact portion 5 provided between the exhaust port 4 and injection nozzles 6 and 7 for injecting cleaning water into the gas-liquid contact portion 5.
  • the air introduced into the housing 2 from the air inlet 3 and the cleaning water sprayed from the spray nozzles 6 and 7 come into contact with each other at the gas-liquid contact portion 5 to clean the air. Is possible. Details of the gas-liquid contact portion 5 and the injection nozzles 6 and 7 will be described later.
  • the air purification apparatus 1 includes a circulation tank 8 that stores the wash water, a circulation pump 9 that circulates the wash water by supplying the wash water in the circulation tank 8 to the injection nozzles 6 and 7, and a circulation tank 8. And an external water source 10 for supplying cleaning water.
  • the circulation tank 8 is provided in the lower part of the housing
  • the circulation pump 9 has a primary side (suction side) connected to the circulation tank 8 via a pipe 11 and a secondary side (discharge side) connected to the injection nozzles 6 and 7 via a pipe 12. Wash water can be circulated.
  • the external water source 10 is connected to the inside of the housing 2 through a pipe 13 and can be replenished with washing water from the external water source 10 by controlling a water supply valve 14 provided in the pipe 13. Further, since the drain valve 15 for draining water is connected to the bottom surface of the circulation tank 8, the cleaning water can be replaced as necessary.
  • the circulation pump 9 is provided outside the housing 2.
  • the circulation pump 9 may be provided inside the housing 2 as long as it is configured to circulate cleaning water.
  • the circulation pump 9 may be a submersible pump provided in the circulation tank 8.
  • the external water source 10 can clean the gas-liquid contact portion 5 and the eliminator 16 described later with supplementary water (for example, wash away the captured fine particles and gaseous substances).
  • supplementary water for example, wash away the captured fine particles and gaseous substances.
  • the circulation tank 8 and the circulation pump 9 are not necessarily provided, and the cleaning water that has come into contact with air at the gas-liquid contact portion 5 may be drained as it is.
  • the air purification device 1 includes an eliminator (drip-proof plate) 16 provided between the gas-liquid contact portion 5 and the exhaust port 4, and a blower provided to face the exhaust port 4 outside the housing 2. 17.
  • the eliminator 16 has a function of preventing the spray water from scattering from the spray nozzle 7.
  • the blower 17 only needs to be able to introduce external air from the intake port 3 and discharge the air that has passed through the gas-liquid contact portion 5 from the exhaust port 4. Air may be pushed into the housing 2.
  • the blower 17 may be provided inside the housing 2.
  • a humidity adjusting means such as a desiccant rotor may be provided between the eliminator 16 and the exhaust port 4 in order to remove a large amount of moisture contained in the air purified by the gas-liquid contact method.
  • the washing water stored in the circulation tank 8 is supplied to the injection nozzles 6 and 7 by the circulation pump 9 and is injected to the gas-liquid contact portion 5 by the injection nozzles 6 and 7.
  • the blower 17 when the blower 17 is activated, the inside of the housing 2 is in a reduced pressure state, and the air to be purified is introduced from the air inlet 3 into the housing 2.
  • the introduced air flows in the horizontal direction inside the housing 2 by the blower 17 and reaches the gas-liquid contact portion 5.
  • the air that has reached the gas-liquid contact portion 5 makes gas-liquid contact with the cleaning water at the gas-liquid contact portion 5, and particulate matter and gaseous chemical substances in the air are removed by the cleaning water.
  • FIG. 2 is a cross-sectional view showing a configuration example of the injection nozzle of the present embodiment.
  • the gas-liquid contact portion 5 is not particularly limited as long as it is a filler that realizes gas-liquid contact between air and washing water, but has a low pressure loss and a high removal performance of fine particles and gaseous substances. In view of achieving compatibility and achieving downsizing in the horizontal direction, it is preferably made of a mat-like fiber assembly.
  • the raw material of the fibers constituting the fiber assembly may be any material that can be processed into fibers, for example, polyamides such as wholly aromatic polyamide, nylon 6 and nylon 66; polyesters such as polyethylene terephthalate and polybutylene terephthalate; Poly (halogenated olefins) such as vinyl, polyvinylidene chloride, polyvinylidene fluoride, and polytetrafluoroethylene; Nitrile monomers such as polyacrylonitrile and polymethacrylonitrile; Polyvinyl such as polyvinyl acetate, vinyl polypropionate, and polyvinyl alcohol Examples thereof include esters and hydrolysis products thereof; celluloses such as cellulose, acetylcellulose, and rayon; and polyolefins such as polyethylene, polypropylene, and ethylene-vinyl acetate copolymer.
  • polyamides such as wholly aromatic polyamide, nylon 6 and nylon 66
  • polyesters such as polyethylene terephthalate and poly
  • Saran Lock (registered trademark) of Asahi Kasei Home Products Corporation can be mentioned.
  • Saran lock is a three-dimensional nonwoven fabric obtained by curling Saran (registered trademark) fiber, which is a highly flame-retardant fiber of the material itself, into a nonwoven fabric by curling it into a spring shape and coating and bonding with Saran latex.
  • Saran lock is suitably used because it has a large space and surface area, low ventilation resistance, excellent filtration efficiency, and a large dust collection capacity.
  • those having high water repellency are more preferable, and those having a contact angle with water on the surface of the fiber aggregate of 70 ° or more are preferable.
  • the gas-liquid contact part 5 is disposed so that the lower end thereof is immersed in the cleaning water in the circulation tank 8. Thereby, it is suppressed that the gas-liquid contact part 5 is excessively water-retained (water-sealed) by the jetted cleaning water due to the capillary phenomenon, and an increase in pressure loss can be suppressed.
  • the injection nozzles 6 and 7 are respectively provided on the upstream side and the downstream side of the gas-liquid contact portion 5 with respect to the air flow direction (hereinafter also simply referred to as “upstream side” and “downstream side”, respectively).
  • the injection nozzles 6 and 7 include a front injection nozzle 6 that injects cleaning water onto the upstream surface of the gas-liquid contact portion 5 (hereinafter referred to as “front surface”) and a downstream surface of the gas-liquid contact portion 5 (hereinafter referred to as “front surface”). And a back spray nozzle 7 for spraying cleaning water on the back surface).
  • Each of the injection nozzles 6 and 7 is connected to, for example, an opening formed in a pipe (not shown) provided along the width direction of the gas-liquid contact portion 5 (the width direction of the air flow path).
  • Both the front spray nozzle 6 and the back spray nozzle 7 are arranged in the vicinity of the water surface of the circulation tank 8 and are configured to spray the cleaning water in a plane from the lower side to the upper side in a direction intersecting the air flow direction.
  • the “planar shape” includes a curtain shape, a film shape, a sheet shape, a fan shape, and the like.
  • the cleaning water sprayed in a planar shape from the spray nozzles 6, 7 comes into contact with the air to be treated, or the spray water flow from below or the air flow accompanying the spray water flow causes the horizontal direction As the air flowing through the air diffuses, the chance of contact between the air to be treated and the cleaning water can be increased, and the gas-liquid contact efficiency can be improved. As a result, high removal performance can be exerted on fine particles and gaseous substances.
  • the use of the spray nozzles 6 and 7 for spraying the cleaning water in a planar shape from below is also advantageous in that the number of nozzles necessary to wet the gas-liquid contact portion 5 uniformly can be reduced.
  • the angle formed between the air flow direction and the washing water spray direction is preferably 65 to 90 °, and more preferably 75 to 85 °.
  • the front spray nozzle 6 may be capable of changing the spray direction of the cleaning water according to the flow velocity or flow rate of the air flowing through the housing 2. For example, when the flow rate of air is high, it is possible to inject cleaning water from a vertical direction (upward) to a direction inclined upstream. Thereby, even if the flow velocity of air changes, it becomes possible to wet the gas-liquid contact part 5 appropriately by changing the jet direction of washing water according to it.
  • a method for measuring the flow velocity of air a method of calculating from the differential pressure between the inlet pressure (pressure at the intake port 3) and the outlet pressure (pressure at the exhaust port 4) can be used.
  • the air flow rate can be measured by a flow meter.
  • the injection nozzles 6 and 7 are only required to be able to inject the cleaning water in a plane in a direction intersecting the air flow direction from below to above with respect to the air flow. It is preferable to have a configuration as shown. That is, the injection nozzles 6 and 7 are in communication with the pipe, the supply flow path 21 to which the cleaning water is supplied, and the injection flow path 22 in communication with the supply flow path 21 and having a diameter smaller than the diameter of the supply flow path 21.
  • an inclined guide surface 23 that is provided at a position opposite to the injection opening 22a of the injection flow path 22 and is inclined with respect to the axis L of the injection flow path 22, and is configured to incline guide the cleaning water injected from the injection opening 22a. It is preferable to have an inclined guide surface 23 that jets cleaning water in a planar shape by guiding the surface 23 to the outside. Thereby, the water which is mist-like and has a small particle diameter can be jetted in a planar shape, so that the gas-liquid contact portion 5 can be efficiently wetted.
  • a fan-type spray nozzle that has a small amount of spray water, can disperse the spray water, and can spray water over a wide range while the spray pressure is small is suitable.
  • a fan-shaped spray nozzle for example, a wide-angle fan-shaped nozzle (YYP series) manufactured by Ikeuchi Co., Ltd. may be mentioned. Only one injection nozzle 6, 7 may be arranged at the center in the width direction of the gas-liquid contact portion 5 (the width direction of the air flow path), or a plurality of injection nozzles may be arranged along the width direction.
  • YYP series wide-angle fan-shaped nozzle
  • washing water injection means with respect to the gas-liquid contact part 5, it is not limited to what injects washing water with the nozzle connected to the opening part of the above pipes, For example, it was provided in the pipe
  • the cleaning water may be directly jetted from a plurality of slits or holes.
  • a pipe provided with a plurality of slits or holes is installed in the circulation tank 8, and a gas such as air is supplied into the pipe, so that the cleaning water in the circulation tank 8 is supplied with the gas from the plurality of slits or holes.
  • a method of spraying can also be used.
  • the washing water jetting unit may be provided at least on the upstream side of the gas-liquid contact portion 5 and is not necessarily provided on the downstream side.
  • the front injection nozzle 6 may be provided, and the back injection nozzle 7 is not necessarily provided.
  • the cleaning water used for purifying the air is not particularly limited as long as it is clean water, and tap water, well water, distilled water, pure water, electrolytic water, and the like can be used.
  • the front spray nozzle 6 and the back spray nozzle 7 spray the same cleaning water, but it is not always necessary, and different cleaning water may be sprayed.
  • the front spray nozzle 6 may spray the circulating water in the circulation tank 8, and the back spray nozzle 7 may spray new water (replenishment water) from the external water source 10.
  • the washing water may be jetted at a high temperature, and the back jet nozzle 7 may jet the washing water at a low temperature.
  • the front spray nozzle 6 may spray acidic water
  • the back spray nozzle 7 may spray alkaline hypochlorous acid water.
  • the wash water after use may be drained as it is, or may be collected, collected, reprocessed and reused.
  • the gas-liquid contact portion 5 is preferably inclined forward toward the upstream side with respect to the air flow direction, that is, inclined so that the upper portion is located upstream from the lower portion. Preferably it is.
  • Such a forward tilting arrangement has not only the effect of improving the gas-liquid contact efficiency by increasing the contact opportunity between the air to be treated and the cleaning water in the gas-liquid contact portion 5, but also has the following effect. Due to the flow of air flowing into the housing 2, a part of the cleaning water sprayed from the front spray nozzle 6 is refined and scattered downstream.
  • Such fine water droplets can not only efficiently wet the gas-liquid contact portion 5 but also come into contact with the air to take in fine particles and gaseous substances contained in the air, and the water droplet diameter and water droplet mass. It can flow down while increasing. Since the gas-liquid contact part 5 is inclined forward to the upstream side, a constant space is formed between the cleaning water sprayed from the front spray nozzle 6 and the gas-liquid contact part 5, and as a result, a fine space is formed. The area where the converted water droplets are scattered increases. In addition to this, since the gas-liquid contact part 5 is inclined forward, the flow rate of the washing water is slowed down in the gas-liquid contact part 5, the flow direction is dispersed by the filler, and there is no bias. A water retention state is realized. Thereby, the contact opportunity of to-be-processed air and washing water increases, and it becomes possible to improve a particulate removal rate and a gaseous substance removal rate.
  • the gas-liquid contact part 5 is inclined forward is that the ejection distance of the front spray nozzle 6 that is indispensable as washing water spraying means for the gas-liquid contact part 5 (for example, the front of the gas-liquid contact part 5 from the nozzle tip) It is also advantageous in that the distance to the upper end can be shortened. That is, by shortening the injection distance, it can be made less susceptible to the influence of air flow, and the injection pressure can be reduced.
  • the inclination angle of the gas-liquid contact portion 5 is preferably 60 to 85 °.
  • the gas-liquid contact part 5 When the gas-liquid contact part 5 is inclined forward to the upstream side, it is preferable that the gas-liquid contact part 5 is in line contact with the inner upper surface of the housing 2. It is preferable to form a space between them. Specifically, as illustrated, the upper end of the back surface of the gas-liquid contact portion 5 and the inner upper surface of the housing 2 are in line contact, and the upper surface of the gas-liquid contact portion 5 and the inner upper surface of the housing 2 are in between. It is preferable that an open space is formed on the upstream side. By forming such a space, the cleaning water is easily held on the upper part of the gas-liquid contact portion 5 when the cleaning water is jetted from the front injection nozzle 6 toward the gas-liquid contact portion 5.
  • the gas-liquid contact portion 5 is a member having a rectangular cross section.
  • the cross section has another geometric shape, if the upstream surface is inclined forward, the same as described above. An effect can be obtained. That is, it is preferable that the gas-liquid contact part 5 has an inclined surface that is inclined so that the upper part is located upstream of the lower part on the upstream side.
  • a water film is formed by the wash water sprayed continuously, and fine bubbles may be continuously generated by embracing the air flowing through the water film.
  • the gas-liquid contact efficiency can be improved by the generation of such fine bubbles.
  • the contact angle of the cleaning water with respect to the front surface of the gas-liquid contact portion 5 is preferably 5 to 30 °, and more preferably 10 to 20 °. Further, the contact angle of the cleaning water with respect to the back surface of the gas-liquid contact portion 5 is preferably 5 to 30 °. Thereby, generation
  • the air purifying device 1 is the water protruding downward from the inner upper surface of the housing 2 on the upstream side of the front injection nozzle 6. It is preferable to have a return portion 18 and a fiber sheet 19 that hangs down from the tip of the water return portion 18 to the vicinity of the water surface of the circulation tank 8. With such a configuration, the water droplets scattered on the upstream side are returned to the lower side by the water return unit 18 or captured by the fiber sheet 19 to be used for gas-liquid contact with the air to be treated. Can do.
  • FIG. 3 is a schematic view showing another configuration example of the air purification device of the present embodiment.
  • the same reference numerals in some cases, subscript symbols
  • FIG. 3 for the sake of simplicity, some components are not shown.
  • the air purification apparatus 1 of the present embodiment includes a plurality (four in the illustrated example) of gas-liquid contact portions 5a to 5d and a plurality of pairs (four in the illustrated example) of the injection nozzles 6a to 6d, 7a to 7d, which are accommodated in a plurality (two in the illustrated example) of the casings 2a and 2b.
  • one gas-liquid contact portion 5a and a pair of jet nozzles 6a and 7a are accommodated in the first housing 2a
  • the three gas-liquid contact portions 5b to 5d are accommodated in the second housing 2b.
  • three pairs of injection nozzles 6b to 6d and 7b to 7d are accommodated.
  • the exhaust port 4a of the first casing 2a and the intake port 3b of the second casing 2b are connected in series by a pipe or the like, and are discharged from the first casing 2a.
  • the air is introduced into the second housing 2b.
  • the three gas-liquid contact portions 5b to 5d accommodated in the second casing 2b are arranged in a line along the air flow direction.
  • the degree of contamination concentration and particle diameter of pollutants contained in the air
  • temperature, humidity, vapor pressure, air volume, wind speed and pressure the gas-liquid contact parts 5a to 5d
  • the configuration for example, the specific surface area of the fibers constituting the fiber assembly
  • One circulation pump for circulating the cleaning water may be provided for each of the casings 2a and 2b, or may be provided only for the second casing 2b. Further, the second casing 2b may be provided with a plurality of circulation pumps, for example, to circulate cleaning water for each of the gas-liquid contact portions 5b to 5d.
  • the circulation tank 8b of the second housing 2b is divided into a plurality of small tanks by partitioning a plate-shaped member, a slit-containing plate material, a filter, a semipermeable membrane or the like according to the number of gas-liquid contact portions 5b to 5d. It may be divided. In that case, for example, a step may be provided between the small tanks so that the washing water flows with a height difference from the downstream side to the upstream side.
  • the hole diameter of each filter may become small gradually as it goes downstream.
  • the plurality of gas-liquid contact portions 5a to 5d are arranged in a line along the air flow path, but the gas-liquid contact parts are arranged in a line in a direction intersecting the air flow path. Also good. Thereby, parallel processing of air to be processed is possible, and it is possible to cope with an increase in the processing air volume.
  • the gas-liquid contact portions may be two-dimensionally stacked in two directions in a horizontal plane, or three-dimensionally stacked in the vertical direction. May be arranged.
  • the gas-liquid contact part is arrange
  • Example 1 the methanol removal rate (change in the concentration of methanol gas) by the air purification process was measured using the air purification apparatus of the first embodiment.
  • the water purifier and the fiber sheet are not provided in the air purifier used in the present Example.
  • the casing a housing that forms an internal space with a width of 170 mm, a height of 300 mm, and a depth of 350 mm is used.
  • the gas-liquid contact portion the thickness is 20 mm
  • the width is 170 mm
  • the fiber fineness is 75 denier
  • the specific surface area is An 890 m 2 / m 3 Saran lock (product number: CS-120) was used, and the angle between the front surface and the horizontal plane was 90 °.
  • Saran lock (product number: CS-120) having a fiber fineness of 75 denier, a thickness of 20 mm, a width of 170 mm, and a specific surface area of 890 m 2 / m 3 was used.
  • a wide-angle fan-shaped nozzle (model number: 1/8 MYP030PVC) manufactured by Ikeuchi Co., Ltd. was used as the spray nozzle, and one nozzle was arranged at the center in the width direction of the housing.
  • the direction of spraying the washing water from the spray nozzle was set vertically upward and the spray flow rate was 3 L / min.
  • methanol gas whose gas concentration was adjusted to 400 ppm by an impinger was used, and the treatment air flow rate was 36 m 3 / h.
  • the methanol removal rate was calculated from the methanol concentration of the air to be treated and the methanol concentration of the purified air by the detection tubes provided on the upstream side of the intake port and the downstream side of the exhaust port, respectively.
  • the differential pressure was measured as a pressure difference between the upstream side of the intake port and the downstream side of the exhaust port using a differential pressure gauge.
  • Example 2 The methanol removal rate was measured under the same conditions as in Example 1 except that the angle between the front surface of the fiber assembly and the horizontal plane was 80 °.
  • Example 1 Methanol is used under the same conditions as in Example 1 except that a full cone nozzle (model number: 1/8 MINJJX030PP (FEPM) + PPS) manufactured by Ikeuchi Co., Ltd. is used as the injection nozzle and is arranged in front and rear of the gas-liquid contact portion. The removal rate was measured.
  • a full cone nozzle model number: 1/8 MINJJX030PP (FEPM) + PPS
  • Comparative Example 2 The methanol removal rate was measured under the same conditions as in Comparative Example 1 except that the angle between the front surface of the fiber assembly and the horizontal plane was 80 °. Table 1 shows the results of methanol removal rate and differential pressure in Example 1, Example 2, Comparative Example 1, and Comparative Example 2.
  • Example 1 and Example 2 compared to Comparative Example 1 and Comparative Example 2, it was confirmed that good results were obtained in both methanol removal rate and differential pressure. This is due to the difference in the jet form of the wash water, and is considered to be the effect of jetting the wash water from the bottom to the gas-liquid contact portion from below. On the other hand, when Example 1 and Example 2 are compared, Example 2 is better in terms of the methanol removal rate. This is because the gas-liquid contact portion is inclined forward with respect to the air flow direction. This is considered to be the effect.

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Abstract

An air purification device 1 has: an intake port 3 and an exhaust port 4 provided to a housing 2 so that air flows in a horizontal direction through the inside of the housing 2; an air/liquid contact part 5 for bringing air introduced into the housing 2 from the intake port 3 into contact with washing water, the air/liquid contact part 5 being provided between the intake port 3 and the exhaust port 4; and a washing water jetting means 6 for jetting the washing water in planar fashion in a direction upwardly intersecting with a flow direction of air, the washing water jetting means 6 being provided on an upstream side of the air/liquid contact part 5 with respect to the flow direction of air.

Description

空気浄化装置Air purification device
 本発明は、空気浄化装置に関する。 The present invention relates to an air purification device.
 従来から、洗浄水と空気とを接触させることで、空気に含まれる微粒子やガス状物質等を除去する空気浄化装置が用いられている。このような気液接触方式の空気浄化装置としては、ビルの空調機や外調機、各種製品の製造に伴う排ガスの除塵や脱臭用などに用いられているスクラバーが知られている。そのなかでも、特に、ラシヒリングやテラレットパッキン、繊維集合体などの充填材を用いた充填式スクラバーが知られている。
 充填式スクラバーは、大きく縦型(垂直型)と横型(水平型)の2つに分類される。縦型スクラバーは、充填材に対して空気が下方から上方に垂直方向に流れるように構成されたスクラバーであり、横型スクラバーは、充填材に対して空気が水平方向に流れるように構成されたスクラバーである。
2. Description of the Related Art Conventionally, air purifiers that remove fine particles or gaseous substances contained in air by bringing cleaning water into contact with air have been used. As such a gas-liquid contact type air purifier, scrubbers used for building air conditioners and external air conditioners, and for dust removal and deodorization of exhaust gas in the manufacture of various products are known. Among them, in particular, a filling scrubber using a filler such as Raschig ring, terralet packing, or a fiber assembly is known.
Filling scrubbers are roughly classified into two types: vertical (vertical) and horizontal (horizontal). The vertical scrubber is a scrubber configured such that air flows vertically from below to the filler, and the horizontal scrubber is configured such that air flows horizontally relative to the filler. It is.
 縦型スクラバーは、各種製品の製造に伴う排ガスの除塵や脱臭用など、産業用に多く適用されている。しかしながら、充填層の高さが高くなり、装置が大型化するため、家庭用、すなわち、一戸建てや集合住宅などの住宅において居住空間に導入する外気や居住空間を循環する空気を浄化するための用途としては好ましくない。また、縦型スクラバーは、充填材において洗浄水の流れ(下向き)と空気の流れ(上向き)とが向流である。そのため、空気の流量を増加させていくと、最終的に洗浄水が下向きに流れなくなるフラッディングが発生し、気液接触が十分に行われなくなるという問題もある。これに対し、横型スクラバーは、充填材において洗浄水の流れ(下向き)と空気の流れ(横向き)とが垂直である。そのため、それらの流れが干渉しにくく、フラッディングの発生を抑制することができるという利点があり、様々な用途に好適に用いられている。
 横型スクラバーにおいて、充填材に洗浄水を供給する方法としては、充填材の前方(空気の流れ方向の上流側)や充填材の上方に設けられた複数のノズルから、それぞれ洗浄水を噴射する方法が知られている(例えば、特許文献1,2参照)。
Vertical scrubbers are widely used for industrial purposes, such as dust removal and deodorization of exhaust gas associated with the manufacture of various products. However, because the height of the packed bed is increased and the apparatus is enlarged, it is used for home use, that is, for purifying the outside air introduced into the living space and the air circulating in the living space in a house such as a detached house or an apartment house. It is not preferable. In the vertical scrubber, the flow of cleaning water (downward) and the flow of air (upward) are countercurrent in the filler. For this reason, when the air flow rate is increased, there is a problem that flooding that eventually causes the washing water not to flow downward occurs, and gas-liquid contact is not sufficiently performed. On the other hand, in the horizontal scrubber, the flow of washing water (downward) and the flow of air (laterally) are vertical in the filler. Therefore, there is an advantage that the flows are less likely to interfere and the occurrence of flooding can be suppressed, and the present invention is suitably used for various applications.
In a horizontal scrubber, as a method of supplying cleaning water to the filler, a method of injecting cleaning water from a plurality of nozzles provided in front of the filler (upstream in the air flow direction) or above the filler, respectively. Is known (see, for example, Patent Documents 1 and 2).
特開平6-254345号公報JP-A-6-254345 特開2003-227622公報JP 2003-227622 A
 洗浄水の噴射形態としては、通常、各ノズルから洗浄水を円錐状や角錐状に噴射する方法が用いられる。微粒子やガス状物質等に対して高い除去性能を発揮させるためには、充填材を十分に濡らす必要があるが、洗浄水を円錐状や角錐状に噴射する方法では、ノズルと気液接触部との水平方向の距離を十分に確保する必要がある。その結果、設置スペースが大きくなってしまい、装置の大型化につながってしまう。
 そこで本発明は、装置の小型化を実現しながら、空気に含まれる微粒子やガス状物質を高効率で除去する空気浄化装置を提供することを目的とする。
As the washing water injection mode, a method of jetting the washing water from each nozzle in a conical shape or a pyramid shape is usually used. In order to exert high removal performance on fine particles, gaseous substances, etc., it is necessary to wet the filler sufficiently, but in the method of spraying cleaning water into a cone or pyramid, the nozzle and gas-liquid contact part It is necessary to secure a sufficient distance in the horizontal direction. As a result, the installation space becomes large, leading to an increase in the size of the apparatus.
SUMMARY OF THE INVENTION An object of the present invention is to provide an air purification apparatus that removes particulates and gaseous substances contained in air with high efficiency while realizing downsizing of the apparatus.
 上述した目的を達成するために、本発明の空気浄化装置は、筐体の内部を空気が水平方向に流れるように筐体に設けられた吸気口および排気口と、吸気口と排気口との間に設けられ、吸気口から筐体内に導入された空気を洗浄水と接触させる気液接触部と、空気の流れ方向に対して気液接触部の上流側に設けられ、下方から上方に向けて上記流れ方向と交差する方向に洗浄水を平面状に噴射する洗浄水噴射手段と、を有している。
 このような空気浄化装置では、気液接触部に対して下方から平面状に洗浄水を噴射するため、気液接触部を十分に濡らすために必要な水平方向の距離を短くすることができる。また、平面状に噴射される洗浄水自体が気液接触を行うことで、被処理空気と洗浄水との接触機会を増加させて気液接触効率を向上させることができる。
In order to achieve the above-described object, an air purification device according to the present invention includes an intake port and an exhaust port provided in a housing such that air flows in a horizontal direction inside the housing, and an intake port and an exhaust port. A gas-liquid contact part that is provided between the gas inlet and the air-liquid contact part for contacting the air introduced into the housing from the intake port with the cleaning water, and is provided upstream of the gas-liquid contact part with respect to the air flow direction. Cleaning water jetting means for jetting cleaning water in a plane in a direction crossing the flow direction.
In such an air purification device, since the cleaning water is jetted from below onto the gas-liquid contact portion, the horizontal distance necessary to sufficiently wet the gas-liquid contact portion can be shortened. Further, since the cleaning water sprayed in a planar shape makes gas-liquid contact, the contact opportunity between the air to be treated and the cleaning water can be increased, and the gas-liquid contact efficiency can be improved.
 以上、本発明によれば、装置の小型化を実現しながら、空気に含まれる微粒子やガス状物質を高効率で除去する空気浄化装置を提供することができる。 As described above, according to the present invention, it is possible to provide an air purification apparatus that removes particulates and gaseous substances contained in air with high efficiency while realizing downsizing of the apparatus.
本発明の第1の実施形態に係る空気浄化装置の構成を示す概略図である。It is the schematic which shows the structure of the air purification apparatus which concerns on the 1st Embodiment of this invention. 本発明の第1の実施形態に係る噴射ノズルの一構成例を示す断面図である。It is sectional drawing which shows one structural example of the injection nozzle which concerns on the 1st Embodiment of this invention. 本発明の第2の実施形態に係る空気浄化装置の構成を示す概略図である。It is the schematic which shows the structure of the air purification apparatus which concerns on the 2nd Embodiment of this invention.
 以下、図面を参照して、本発明の実施の形態について説明する。 Hereinafter, embodiments of the present invention will be described with reference to the drawings.
 本発明の空気浄化装置は、家庭用、すなわち、一戸建てや集合住宅などの住宅において居住空間に導入する外気や居住空間を循環する空気を浄化するための用途として好適に使用することができる。加えて、産業用としても好適に使用することができ、例えば、食品、医薬品、化学製品などの製造工場、紙パルプ工場、飲食業における厨房などからの排気や、畜産業における畜舎、動物実験施設、ごみ置き場・ごみ処理場などからの臭気を処理(浄化、除塵、脱臭など)するための用途として使用することができる。 The air purification device of the present invention can be suitably used for household use, that is, for purifying the outside air introduced into the living space and the air circulating in the living space in a house such as a detached house or a housing complex. In addition, it can also be suitably used for industrial use, for example, exhaust from food, pharmaceutical, chemical product manufacturing factories, pulp and paper factories, food and beverage kitchens, livestock barns, animal experiment facilities, It can be used as an application to treat (purify, remove dust, deodorize, etc.) odors from garbage storage sites and waste disposal sites.
 (第1の実施形態)
 図1は、本発明の第1の実施形態に係る空気浄化装置の構成を示す概略図である。
 空気浄化装置1は、筐体2の内部を空気が水平方向に流れるように構成されたものであり、筐体2の水平方向の両側に設けられた吸気口3および排気口4と、吸気口3と排気口4との間に設けられた気液接触部5と、気液接触部5に洗浄水を噴射する噴射ノズル6,7とを有している。このような構成により、吸気口3から筐体2の内部に導入された空気と噴射ノズル6,7から噴射された洗浄水とが気液接触部5において接触することで、空気を洗浄することが可能になる。気液接触部5および噴射ノズル6,7の詳細については後述する。
(First embodiment)
FIG. 1 is a schematic diagram showing the configuration of the air purification device according to the first embodiment of the present invention.
The air purification device 1 is configured so that air flows in the horizontal direction inside the housing 2, and includes an intake port 3 and an exhaust port 4 provided on both sides of the housing 2 in the horizontal direction, and an intake port. 3 and a gas-liquid contact portion 5 provided between the exhaust port 4 and injection nozzles 6 and 7 for injecting cleaning water into the gas-liquid contact portion 5. With such a configuration, the air introduced into the housing 2 from the air inlet 3 and the cleaning water sprayed from the spray nozzles 6 and 7 come into contact with each other at the gas-liquid contact portion 5 to clean the air. Is possible. Details of the gas-liquid contact portion 5 and the injection nozzles 6 and 7 will be described later.
 また、空気浄化装置1は、洗浄水を貯留する循環タンク8と、循環タンク8内の洗浄水を噴射ノズル6,7に供給することで洗浄水を循環させる循環ポンプ9と、循環タンク8に洗浄水を補給するための外部水源10とを有している。
 循環タンク8は、水面の上方に空気の流れが生じるように筐体2の下部に設けられている。循環ポンプ9は、一次側(吸込側)が配管11を介して循環タンク8に接続され、二次側(吐出側)が配管12を介して噴射ノズル6,7に接続されており、これにより、洗浄水を循環させることができる。外部水源10は、配管13を介して筐体2の内部に接続され、配管13に設けられた給水弁14の制御により、外部水源10から洗浄水を補充することが可能となる。また、循環タンク8の底面に水抜き用の排水弁15が接続されていることで、必要に応じて洗浄水の交換も可能となる。
In addition, the air purification apparatus 1 includes a circulation tank 8 that stores the wash water, a circulation pump 9 that circulates the wash water by supplying the wash water in the circulation tank 8 to the injection nozzles 6 and 7, and a circulation tank 8. And an external water source 10 for supplying cleaning water.
The circulation tank 8 is provided in the lower part of the housing | casing 2 so that the flow of air may arise above the water surface. The circulation pump 9 has a primary side (suction side) connected to the circulation tank 8 via a pipe 11 and a secondary side (discharge side) connected to the injection nozzles 6 and 7 via a pipe 12. Wash water can be circulated. The external water source 10 is connected to the inside of the housing 2 through a pipe 13 and can be replenished with washing water from the external water source 10 by controlling a water supply valve 14 provided in the pipe 13. Further, since the drain valve 15 for draining water is connected to the bottom surface of the circulation tank 8, the cleaning water can be replaced as necessary.
 図示した例では、循環ポンプ9は、筐体2の外部に設けられているが、洗浄水を循環させるようになっていればよく、筐体2の内部に設けられていてもよい。さらに、循環ポンプ9は、循環タンク8内に設けられた水中ポンプであってもよい。また、図示した例では、外部水源10は、補充水によって気液接触部5および後述するエリミネータ16を洗浄する(例えば、取り込んだ微粒子やガス状物質を洗い流す)ことができるように、筐体2の上部に接続されているが、筐体2の下部に接続されて循環タンク8に直接洗浄水を補充するようになっていてもよい。一方で、循環タンク8および循環ポンプ9は必ずしも設けられている必要はなく、気液接触部5で空気と接触した洗浄水をそのまま排水するようになっていてもよい。
 さらに、空気浄化装置1は、気液接触部5と排気口4との間に設けられたエリミネータ(防滴板)16と、筐体2の外側で排気口4に対向して設けられた送風機17とを有している。エリミネータ16は、噴射ノズル7からの噴霧水の飛散を防止する機能を有している。送風機17は、外部の空気を吸気口3から導入し、気液接触部5を通過した空気を排気口4から排出させるようになっていればよく、吸込口3の側に設けられて外部の空気を筺体2内に押し込むようになっていてもよい。また、送風機17は、筐体2の内側に設けられていてもよい。さらに、エリミネータ16と排気口4との間に、気液接触方式により浄化された空気に含まれる大量の湿分を除去するために、デシカントロータなどの湿度調節手段が設けられていてもよい。
In the illustrated example, the circulation pump 9 is provided outside the housing 2. However, the circulation pump 9 may be provided inside the housing 2 as long as it is configured to circulate cleaning water. Further, the circulation pump 9 may be a submersible pump provided in the circulation tank 8. Further, in the illustrated example, the external water source 10 can clean the gas-liquid contact portion 5 and the eliminator 16 described later with supplementary water (for example, wash away the captured fine particles and gaseous substances). However, it may be connected to the lower part of the housing 2 so that the circulation tank 8 is directly replenished with washing water. On the other hand, the circulation tank 8 and the circulation pump 9 are not necessarily provided, and the cleaning water that has come into contact with air at the gas-liquid contact portion 5 may be drained as it is.
Furthermore, the air purification device 1 includes an eliminator (drip-proof plate) 16 provided between the gas-liquid contact portion 5 and the exhaust port 4, and a blower provided to face the exhaust port 4 outside the housing 2. 17. The eliminator 16 has a function of preventing the spray water from scattering from the spray nozzle 7. The blower 17 only needs to be able to introduce external air from the intake port 3 and discharge the air that has passed through the gas-liquid contact portion 5 from the exhaust port 4. Air may be pushed into the housing 2. The blower 17 may be provided inside the housing 2. Further, a humidity adjusting means such as a desiccant rotor may be provided between the eliminator 16 and the exhaust port 4 in order to remove a large amount of moisture contained in the air purified by the gas-liquid contact method.
 ここで、空気浄化装置1を用いた空気浄化動作について簡単に説明する。循環タンク8内に貯留された洗浄水は、循環ポンプ9によって噴射ノズル6,7に供給され、噴射ノズル6,7によって気液接触部5に噴射される。一方、送風機17が作動すると、筐体2内部が減圧状態となり、浄化すべき空気が吸気口3から筐体2内へと導入される。導入された空気は、送風機17によって筐体2の内部を水平方向に流れ、気液接触部5に到達する。気液接触部5に到達した空気は、気液接触部5で洗浄水と気液接触を行い、空気中の粒子性物質やガス状化学物質が洗浄水によって除去される。浄化された空気は、送風機17によって排気口4から排出される。
 次に、気液接触部5および噴射ノズル6,7の詳細について説明する。図2は、本実施形態の噴射ノズルの一構成例を示す断面図である。
Here, the air purification operation using the air purification device 1 will be briefly described. The washing water stored in the circulation tank 8 is supplied to the injection nozzles 6 and 7 by the circulation pump 9 and is injected to the gas-liquid contact portion 5 by the injection nozzles 6 and 7. On the other hand, when the blower 17 is activated, the inside of the housing 2 is in a reduced pressure state, and the air to be purified is introduced from the air inlet 3 into the housing 2. The introduced air flows in the horizontal direction inside the housing 2 by the blower 17 and reaches the gas-liquid contact portion 5. The air that has reached the gas-liquid contact portion 5 makes gas-liquid contact with the cleaning water at the gas-liquid contact portion 5, and particulate matter and gaseous chemical substances in the air are removed by the cleaning water. The purified air is discharged from the exhaust port 4 by the blower 17.
Next, details of the gas-liquid contact portion 5 and the injection nozzles 6 and 7 will be described. FIG. 2 is a cross-sectional view showing a configuration example of the injection nozzle of the present embodiment.
 気液接触部5は、空気と洗浄水との気液接触を実現する充填材であれば、その種類に特に制限はないが、低い圧力損失と微粒子やガス状物質等の高い除去性能とを両立でき、水平方向における小型化を図れる点で、マット状の繊維集合体から構成されていることが好ましい。
 繊維集合体を構成する繊維の原材料としては、繊維に加工できる物質であればよく、例えば、全芳香族ポリアミド、ナイロン6、ナイロン66等のポリアミド;ポリエチレンテレフタレート、ポリブチレンテレフタレート等のポリエステル;ポリ塩化ビニル、ポリ塩化ビニリデン、ポリフッ化ビニリデン、ポリテトラフルオロエチレン等のポリ(ハロゲン化オレフィン);ポリアクリロニトリル、ポリメタクリロニトリル等のニトリル系モノマー;ポリ酢酸ビニル、ポリプロピオン酸ビニル、ポリビニルアルコール等のポリビニルエステルおよびその加水分解生成物;セルロース、アセチルセルロース、レーヨン等のセルロース類;ポリエチレン、ポリプロピレン、エチレン-酢酸ビニル共重合体等のポリオレフィンが挙げられる。
The gas-liquid contact portion 5 is not particularly limited as long as it is a filler that realizes gas-liquid contact between air and washing water, but has a low pressure loss and a high removal performance of fine particles and gaseous substances. In view of achieving compatibility and achieving downsizing in the horizontal direction, it is preferably made of a mat-like fiber assembly.
The raw material of the fibers constituting the fiber assembly may be any material that can be processed into fibers, for example, polyamides such as wholly aromatic polyamide, nylon 6 and nylon 66; polyesters such as polyethylene terephthalate and polybutylene terephthalate; Poly (halogenated olefins) such as vinyl, polyvinylidene chloride, polyvinylidene fluoride, and polytetrafluoroethylene; Nitrile monomers such as polyacrylonitrile and polymethacrylonitrile; Polyvinyl such as polyvinyl acetate, vinyl polypropionate, and polyvinyl alcohol Examples thereof include esters and hydrolysis products thereof; celluloses such as cellulose, acetylcellulose, and rayon; and polyolefins such as polyethylene, polypropylene, and ethylene-vinyl acetate copolymer.
 例えば、上述した繊維集合体としては、旭化成ホームプロダクツ株式会社のサランロック(登録商標)が挙げられる。サランロックは、素材自体が非常に高い難燃繊維であるサラン(登録商標)繊維を、スプリング状にカール加工して不織布状に加工し、サランラテックスで被覆結合した三次元不織布である。サランロックは、大きな空間と表面積を合わせ持ち、通気抵抗が小さく、濾過効率に優れ、しかも集塵容量が大きな構造を備えている点で好適に用いられる。また、上述した繊維集合体としては、撥水性の高いものがより好ましく、繊維集合体表面の水に対する接触角が70°以上のものが好ましい。
 気液接触部5は、その下端が循環タンク8内の洗浄水に浸されるように配置されていることが好ましい。これにより、毛細管現象が生じることで、噴射される洗浄水により気液接触部5が過度に保水(水封)されることが抑制され、圧力損失の上昇を抑えることができる。
For example, as the fiber assembly described above, Saran Lock (registered trademark) of Asahi Kasei Home Products Corporation can be mentioned. Saran lock is a three-dimensional nonwoven fabric obtained by curling Saran (registered trademark) fiber, which is a highly flame-retardant fiber of the material itself, into a nonwoven fabric by curling it into a spring shape and coating and bonding with Saran latex. Saran lock is suitably used because it has a large space and surface area, low ventilation resistance, excellent filtration efficiency, and a large dust collection capacity. Further, as the above-described fiber aggregate, those having high water repellency are more preferable, and those having a contact angle with water on the surface of the fiber aggregate of 70 ° or more are preferable.
It is preferable that the gas-liquid contact part 5 is disposed so that the lower end thereof is immersed in the cleaning water in the circulation tank 8. Thereby, it is suppressed that the gas-liquid contact part 5 is excessively water-retained (water-sealed) by the jetted cleaning water due to the capillary phenomenon, and an increase in pressure loss can be suppressed.
 噴射ノズル6,7は、空気の流れ方向に対して気液接触部5の上流側および下流側(以下、それぞれ単に「上流側」および「下流側」ともいう)にそれぞれ設けられている。噴射ノズル6,7は、気液接触部5の上流側の表面(以下、「前面」という)に洗浄水を噴射する前面噴射ノズル6と、気液接触部5の下流側の表面(以下、「背面」という)に洗浄水を噴射する背面噴射ノズル7とを含んでいる。各噴射ノズル6,7は、例えば、気液接触部5の幅方向(空気流路の幅方向)に沿って設けられたパイプ(図示せず)に形成された開口部に接続されている。
 前面噴射ノズル6と背面噴射ノズル7は、いずれも循環タンク8の水面近傍に配置され、下方から上方に向けて空気の流れ方向と交差する方向に洗浄水を平面状に噴射するように構成されている。なお、ここで「平面状」とは、カーテン状、膜状、シート状、扇形状などを含むことに留意されたい。これにより、気液接触部5に対して、例えば前方および後方から円錐状や角錐状に洗浄水を噴射する場合と比べて、より短い距離で広範囲に洗浄水を噴射することが可能になる。その結果、気液接触部5と噴射ノズル6,7との水平方向の距離を短くすることができ、水平方向における省スペース化を実現することができる。さらに、気液接触部5とは別に、噴射ノズル6,7から平面状に噴射される洗浄水自体が被処理空気と接触したり、下方からの噴射水流や噴射水流に同伴する気流により水平方向に流れる空気が拡散されたりすることにより、被処理空気と洗浄水との接触機会を増加させて気液接触効率を向上させることができる。その結果、微粒子やガス状物質に対して高い除去性能を発揮させることができる。なお、下方から平面状に洗浄水を噴射する噴射ノズル6,7を用いることは、気液接触部5を均一に濡らすために必要なノズル本数を減らせる点でも有利である。
The injection nozzles 6 and 7 are respectively provided on the upstream side and the downstream side of the gas-liquid contact portion 5 with respect to the air flow direction (hereinafter also simply referred to as “upstream side” and “downstream side”, respectively). The injection nozzles 6 and 7 include a front injection nozzle 6 that injects cleaning water onto the upstream surface of the gas-liquid contact portion 5 (hereinafter referred to as “front surface”) and a downstream surface of the gas-liquid contact portion 5 (hereinafter referred to as “front surface”). And a back spray nozzle 7 for spraying cleaning water on the back surface). Each of the injection nozzles 6 and 7 is connected to, for example, an opening formed in a pipe (not shown) provided along the width direction of the gas-liquid contact portion 5 (the width direction of the air flow path).
Both the front spray nozzle 6 and the back spray nozzle 7 are arranged in the vicinity of the water surface of the circulation tank 8 and are configured to spray the cleaning water in a plane from the lower side to the upper side in a direction intersecting the air flow direction. ing. Here, it should be noted that the “planar shape” includes a curtain shape, a film shape, a sheet shape, a fan shape, and the like. Thereby, compared with the case where cleaning water is sprayed with respect to the gas-liquid contact part 5 from front and back, for example in the shape of a cone or a pyramid, it becomes possible to inject cleaning water over a wide range at a shorter distance. As a result, the horizontal distance between the gas-liquid contact portion 5 and the spray nozzles 6 and 7 can be shortened, and space saving in the horizontal direction can be realized. Further, separately from the gas-liquid contact portion 5, the cleaning water sprayed in a planar shape from the spray nozzles 6, 7 comes into contact with the air to be treated, or the spray water flow from below or the air flow accompanying the spray water flow causes the horizontal direction As the air flowing through the air diffuses, the chance of contact between the air to be treated and the cleaning water can be increased, and the gas-liquid contact efficiency can be improved. As a result, high removal performance can be exerted on fine particles and gaseous substances. Note that the use of the spray nozzles 6 and 7 for spraying the cleaning water in a planar shape from below is also advantageous in that the number of nozzles necessary to wet the gas-liquid contact portion 5 uniformly can be reduced.
 前面噴射ノズル6は、空気の流れ方向と洗浄水の噴射方向とのなす角度が65~90°であることが好ましく、75~85°であることがより好ましい。あるいは、前面噴射ノズル6は、筐体2内を流れる空気の流速または流量に応じて洗浄水の噴射方向が変更可能であってもよい。例えば、空気の流速が大きい場合など、洗浄水を垂直方向(上方)から上流側に傾斜した方向に向かって噴射することも可能である。これにより、空気の流速が変化しても、それに応じて洗浄水の噴射方向を変更することで気液接触部5を適切に濡らすことが可能になる。空気の流速を計測する方法としては、入口圧(吸気口3での圧力)と出口圧(排気口4での圧力)との差圧から算出する方法を用いることができる。また、空気の流量は、流量計によって計測することができる。
 噴射ノズル6,7は、空気の流れに対して下方から上方に向けて空気の流れ方向と交差する方向に洗浄水を平面状に噴射できればよく、その構成に特に制限はないが、図2で示すような構成を有していることが好ましい。すなわち、噴射ノズル6,7は、パイプに連通し、洗浄水が供給される供給流路21と、供給流路21に連通し、供給流路21の径よりも小さい径を有する噴射流路22と、噴射流路22の噴射開口22aに対向する位置に設けられ、噴射流路22の軸線Lに対して傾斜した傾斜案内面23であって、噴射開口22aから噴射された洗浄水を傾斜案内面23に沿って外部に案内することで、洗浄水を平面状に噴射させる傾斜案内面23と、を有していることが好ましい。これにより、霧状で粒径の細かい水を平面状に噴射することができ、そのため、気液接触部5を効率良く濡らすことができる。特に、噴霧水量が少なく、噴霧水を分散化でき、噴霧圧力が小さいながらも広範囲への散水を行うことができる扇形スプレーノズルが好適である。このような扇形スプレーノズルとしては、例えば、株式会社いけうち製の広角扇形ノズル(YYPシリーズ)が挙げられる。噴射ノズル6,7は、それぞれ気液接触部5の幅方向(空気流路の幅方向)の中央に1つだけ配置されていてもよく、幅方向に沿って複数配置されていてもよい。
In the front spray nozzle 6, the angle formed between the air flow direction and the washing water spray direction is preferably 65 to 90 °, and more preferably 75 to 85 °. Alternatively, the front spray nozzle 6 may be capable of changing the spray direction of the cleaning water according to the flow velocity or flow rate of the air flowing through the housing 2. For example, when the flow rate of air is high, it is possible to inject cleaning water from a vertical direction (upward) to a direction inclined upstream. Thereby, even if the flow velocity of air changes, it becomes possible to wet the gas-liquid contact part 5 appropriately by changing the jet direction of washing water according to it. As a method for measuring the flow velocity of air, a method of calculating from the differential pressure between the inlet pressure (pressure at the intake port 3) and the outlet pressure (pressure at the exhaust port 4) can be used. The air flow rate can be measured by a flow meter.
The injection nozzles 6 and 7 are only required to be able to inject the cleaning water in a plane in a direction intersecting the air flow direction from below to above with respect to the air flow. It is preferable to have a configuration as shown. That is, the injection nozzles 6 and 7 are in communication with the pipe, the supply flow path 21 to which the cleaning water is supplied, and the injection flow path 22 in communication with the supply flow path 21 and having a diameter smaller than the diameter of the supply flow path 21. And an inclined guide surface 23 that is provided at a position opposite to the injection opening 22a of the injection flow path 22 and is inclined with respect to the axis L of the injection flow path 22, and is configured to incline guide the cleaning water injected from the injection opening 22a. It is preferable to have an inclined guide surface 23 that jets cleaning water in a planar shape by guiding the surface 23 to the outside. Thereby, the water which is mist-like and has a small particle diameter can be jetted in a planar shape, so that the gas-liquid contact portion 5 can be efficiently wetted. In particular, a fan-type spray nozzle that has a small amount of spray water, can disperse the spray water, and can spray water over a wide range while the spray pressure is small is suitable. As such a fan-shaped spray nozzle, for example, a wide-angle fan-shaped nozzle (YYP series) manufactured by Ikeuchi Co., Ltd. may be mentioned. Only one injection nozzle 6, 7 may be arranged at the center in the width direction of the gas-liquid contact portion 5 (the width direction of the air flow path), or a plurality of injection nozzles may be arranged along the width direction.
 なお、気液接触部5に対する洗浄水噴射手段としては、上述のようなパイプの開口部に接続されたノズルにより洗浄水を噴射するものに限定されるものではなく、例えば、パイプに設けられた複数のスリットまたは孔から洗浄水を直接噴射するものであってもよい。あるいは、複数のスリットまたは孔が設けられたパイプを循環タンク8内に設置し、パイプ内に空気などのガスを供給することで、複数のスリットまたは孔から循環タンク8内の洗浄水をガスと共に噴射させる方法を用いることもできる。また、洗浄水噴射手段としては、少なくとも気液接触部5の上流側に設けられていればよく、下流側には必ずしも設けられている必要はない。すなわち、本実施形態の場合、少なくとも前面噴射ノズル6が設けられていればよく、背面噴射ノズル7は必ずしも設けられている必要はない。
 空気を浄化するために使用する洗浄水としては、清浄な水であれば特に制限はなく、水道水、井水、蒸留水、純水、電解水等を用いることができる。本実施形態では、前面噴射ノズル6と背面噴射ノズル7は、同じ洗浄水を噴射するようになっているが、必ずしもその必要はなく、それぞれ別の洗浄水を噴射するようになっていてもよい。例えば、前面噴射ノズル6が循環タンク8内の循環水を噴射し、背面噴射ノズル7が外部水源10からの新水(補充水)を噴射するようになっていてもよく、前面噴射ノズル6が高温で洗浄水を噴射し、背面噴射ノズル7が低温で洗浄水を噴射するようになっていてもよい。あるいは、前面噴射ノズル6が酸性水を噴射し、背面噴射ノズル7がアルカリ性次亜塩素酸水を噴射するようになっていてもよい。この場合、上述したように、使用後の洗浄水はそのまま排水されてもよく、あるいは、まとめて回収し、再処理して再利用するようになっていてもよい。
In addition, as a washing water injection means with respect to the gas-liquid contact part 5, it is not limited to what injects washing water with the nozzle connected to the opening part of the above pipes, For example, it was provided in the pipe The cleaning water may be directly jetted from a plurality of slits or holes. Alternatively, a pipe provided with a plurality of slits or holes is installed in the circulation tank 8, and a gas such as air is supplied into the pipe, so that the cleaning water in the circulation tank 8 is supplied with the gas from the plurality of slits or holes. A method of spraying can also be used. Further, the washing water jetting unit may be provided at least on the upstream side of the gas-liquid contact portion 5 and is not necessarily provided on the downstream side. That is, in the case of this embodiment, at least the front injection nozzle 6 may be provided, and the back injection nozzle 7 is not necessarily provided.
The cleaning water used for purifying the air is not particularly limited as long as it is clean water, and tap water, well water, distilled water, pure water, electrolytic water, and the like can be used. In the present embodiment, the front spray nozzle 6 and the back spray nozzle 7 spray the same cleaning water, but it is not always necessary, and different cleaning water may be sprayed. . For example, the front spray nozzle 6 may spray the circulating water in the circulation tank 8, and the back spray nozzle 7 may spray new water (replenishment water) from the external water source 10. The washing water may be jetted at a high temperature, and the back jet nozzle 7 may jet the washing water at a low temperature. Alternatively, the front spray nozzle 6 may spray acidic water, and the back spray nozzle 7 may spray alkaline hypochlorous acid water. In this case, as described above, the wash water after use may be drained as it is, or may be collected, collected, reprocessed and reused.
 ところで、気液接触部5は、図示したように、空気の流れ方向に対して上流側に前傾していることが好ましく、すなわち、上部が下部よりも上流側に位置するように傾斜していることが好ましい。このような前傾配置には、気液接触部5において被処理空気と洗浄水との接触機会を増加させて気液接触効率を向上させるという効果だけでなく、次のような効果もある。
 筐体2内に流入する空気の流れによって、前面噴射ノズル6から噴射される洗浄水の一部は微細化して下流側に飛散する。このような微細化した水滴は、気液接触部5を効率的に濡らすことができるだけでなく、それ自体が空気と接触して空気に含まれる微粒子やガス状物質を取り込み、水滴径や水滴質量を増大させながら流れ落ちることができる。気液接触部5が上流側に前傾していることで、前面噴射ノズル6から噴射される洗浄水と気液接触部5との間には一定の空間が形成され、結果的に、微細化した水滴が飛散する領域が増加することになる。これに加えて、気液接触部5が前傾していることで、気液接触部5内では、洗浄水の流下速度が遅くなり、充填材により流下方向も分散され、偏りのない適度な保水状態が実現される。これにより、被処理空気と洗浄水との接触機会が増加して、微粒子除去率やガス状物質除去率を向上させることが可能となる。
By the way, as shown in the drawing, the gas-liquid contact portion 5 is preferably inclined forward toward the upstream side with respect to the air flow direction, that is, inclined so that the upper portion is located upstream from the lower portion. Preferably it is. Such a forward tilting arrangement has not only the effect of improving the gas-liquid contact efficiency by increasing the contact opportunity between the air to be treated and the cleaning water in the gas-liquid contact portion 5, but also has the following effect.
Due to the flow of air flowing into the housing 2, a part of the cleaning water sprayed from the front spray nozzle 6 is refined and scattered downstream. Such fine water droplets can not only efficiently wet the gas-liquid contact portion 5 but also come into contact with the air to take in fine particles and gaseous substances contained in the air, and the water droplet diameter and water droplet mass. It can flow down while increasing. Since the gas-liquid contact part 5 is inclined forward to the upstream side, a constant space is formed between the cleaning water sprayed from the front spray nozzle 6 and the gas-liquid contact part 5, and as a result, a fine space is formed. The area where the converted water droplets are scattered increases. In addition to this, since the gas-liquid contact part 5 is inclined forward, the flow rate of the washing water is slowed down in the gas-liquid contact part 5, the flow direction is dispersed by the filler, and there is no bias. A water retention state is realized. Thereby, the contact opportunity of to-be-processed air and washing water increases, and it becomes possible to improve a particulate removal rate and a gaseous substance removal rate.
 気液接触部5が上流側に前傾していることは、気液接触部5に対する洗浄水噴射手段として必須の前面噴射ノズル6の噴射距離(例えば、ノズル先端から気液接触部5の前面上端までの距離)を短くすることができる点でも有利である。すなわち、噴射距離が短くなることで、空気の流れの影響を受けにくくすることができ、噴射圧力を小さくすることもできる。ただし、気液接触部5が過度に前傾していると、水平方向における小型化という観点からは好ましくない。そのため、気液接触部5の傾斜角度(前面と水平面との角度)は60~85°が好適である。
 気液接触部5が上流側に前傾している場合、気液接触部5は、筐体2の内側上面に線接触していることが好ましく、それにより、筐体2の内側上面との間に空間を形成していることが好ましい。具体的には、図示したように、気液接触部5の背面の上端と筐体2の内側上面とが線接触し、気液接触部5の上面と筐体2の内側上面との間に、上流側に開放する空間が形成されていることが好ましい。このような空間が形成されていることで、前面噴射ノズル6から気液接触部5に向けて洗浄水が噴射される際に、気液接触部5の上部に洗浄水が保持されやすくなる。その結果、重力の影響によって気液接触部5の上部付近に水分が少ない領域が発生することを抑制して、気液接触に影響を与えたり、偏流が誘発されたりする可能性を低減することができる。また、上述の空間に洗浄水が滞留することで、空気が洗浄液と接触せずに気液接触部5を通過してしまうショートパスを抑制することができる。
The fact that the gas-liquid contact part 5 is inclined forward is that the ejection distance of the front spray nozzle 6 that is indispensable as washing water spraying means for the gas-liquid contact part 5 (for example, the front of the gas-liquid contact part 5 from the nozzle tip) It is also advantageous in that the distance to the upper end can be shortened. That is, by shortening the injection distance, it can be made less susceptible to the influence of air flow, and the injection pressure can be reduced. However, if the gas-liquid contact portion 5 is excessively inclined, it is not preferable from the viewpoint of miniaturization in the horizontal direction. Therefore, the inclination angle of the gas-liquid contact portion 5 (angle between the front surface and the horizontal surface) is preferably 60 to 85 °.
When the gas-liquid contact part 5 is inclined forward to the upstream side, it is preferable that the gas-liquid contact part 5 is in line contact with the inner upper surface of the housing 2. It is preferable to form a space between them. Specifically, as illustrated, the upper end of the back surface of the gas-liquid contact portion 5 and the inner upper surface of the housing 2 are in line contact, and the upper surface of the gas-liquid contact portion 5 and the inner upper surface of the housing 2 are in between. It is preferable that an open space is formed on the upstream side. By forming such a space, the cleaning water is easily held on the upper part of the gas-liquid contact portion 5 when the cleaning water is jetted from the front injection nozzle 6 toward the gas-liquid contact portion 5. As a result, it is possible to suppress the occurrence of a region with little moisture near the upper portion of the gas-liquid contact portion 5 due to the influence of gravity, thereby reducing the possibility of affecting gas-liquid contact or inducing drift. Can do. Further, since the cleaning water stays in the above-described space, it is possible to suppress a short path in which air passes through the gas-liquid contact portion 5 without contacting the cleaning liquid.
 図示した例では、気液接触部5は、断面が矩形の部材であるが、例えば断面が他の幾何形状を有する場合、上流側の面が前傾していれば、上述したのと同様の効果を得ることができる。すなわち、気液接触部5は、上流側に、上部が下部よりも上流側に位置するように傾斜した傾斜面を有していることが好ましい。
 なお、気液接触部5の前面では、連続的に噴射される洗浄水により水膜が形成され、その水膜が流通する空気を抱き込むことで微細気泡が連続的に生成されることがあるが、このような微細気泡の発生によっても気液接触効率を向上させることができる。このような観点から、気液接触部5の前面に対する洗浄水の接触角度は、5~30°であることが好ましく、10~20°であることがより好ましい。また、気液接触部5の背面に対する洗浄水の接触角度は、5~30°であることが好ましい。これにより、上述の微細気泡の生成を促進させることができ、気液接触効率をより一層向上させることができる。
In the illustrated example, the gas-liquid contact portion 5 is a member having a rectangular cross section. For example, when the cross section has another geometric shape, if the upstream surface is inclined forward, the same as described above. An effect can be obtained. That is, it is preferable that the gas-liquid contact part 5 has an inclined surface that is inclined so that the upper part is located upstream of the lower part on the upstream side.
In addition, in the front surface of the gas-liquid contact part 5, a water film is formed by the wash water sprayed continuously, and fine bubbles may be continuously generated by embracing the air flowing through the water film. However, the gas-liquid contact efficiency can be improved by the generation of such fine bubbles. From such a viewpoint, the contact angle of the cleaning water with respect to the front surface of the gas-liquid contact portion 5 is preferably 5 to 30 °, and more preferably 10 to 20 °. Further, the contact angle of the cleaning water with respect to the back surface of the gas-liquid contact portion 5 is preferably 5 to 30 °. Thereby, generation | occurrence | production of the above-mentioned fine bubble can be accelerated | stimulated, and gas-liquid contact efficiency can be improved further.
 前面噴射ノズル6から噴射される洗浄水のうち、上述したように、空気の流れによって微細化して下流側に飛散するものもあるが、例えば気液接触部5に当たることで水滴となって上流側に飛散するものもある。このような現象は、特に筐体2の内側上面付近で顕著である。本実施形態では、こうした上流側に飛散する水滴も気液接触に有効に利用するために、空気浄化装置1が、前面噴射ノズル6の上流側で筐体2の内側上面から下方に突出する水返し部18と、水返し部18の先端から循環タンク8の水面近傍まで垂れ下がる繊維シート19とを有していることが好ましい。このような構成により、上流側に飛散する水滴は、水返し部18によって下方に返されたり、繊維シート19で捕捉されたりすることで、被処理空気との気液接触のために利用することができる。 Among the cleaning water sprayed from the front spray nozzle 6, as described above, there are some which are refined by the flow of air and scattered downstream, but for example, contact with the gas-liquid contact portion 5 to form water droplets on the upstream side Some are scattered. Such a phenomenon is particularly prominent near the inner upper surface of the housing 2. In the present embodiment, in order to effectively use the water droplets scattered on the upstream side for the gas-liquid contact, the air purifying device 1 is the water protruding downward from the inner upper surface of the housing 2 on the upstream side of the front injection nozzle 6. It is preferable to have a return portion 18 and a fiber sheet 19 that hangs down from the tip of the water return portion 18 to the vicinity of the water surface of the circulation tank 8. With such a configuration, the water droplets scattered on the upstream side are returned to the lower side by the water return unit 18 or captured by the fiber sheet 19 to be used for gas-liquid contact with the air to be treated. Can do.
 (第2の実施形態)
 図3は、本実施形態の空気浄化装置の他の構成例を示す概略図である。以下、第1の実施形態と同様の構成については、図面に同じ符号(場合によっては添字付きの符号)を付してその説明を省略し、第1の実施形態と異なる構成のみ説明する。なお、図3では、簡単のために、一部の構成は図示を省略している。
 本実施形態の空気浄化装置1は、複数(図示した例では4つ)の気液接触部5a~5dと、これに応じて複数対(図示した例では4対)の噴射ノズル6a~6d,7a~7dとを有し、これらは複数(図示した例では2つ)の筐体2a,2bに収容されている。具体的には、第1の筐体2aに、1つの気液接触部5aと1対の噴射ノズル6a,7aが収容され、第2の筐体2bに、3つの気液接触部5b~5dと3対の噴射ノズル6b~6d,7b~7dが収容されている。
(Second Embodiment)
FIG. 3 is a schematic view showing another configuration example of the air purification device of the present embodiment. Hereinafter, with respect to the same configuration as that of the first embodiment, the same reference numerals (in some cases, subscript symbols) are attached to the drawings, and the description thereof is omitted, and only the configuration different from that of the first embodiment will be described. In FIG. 3, for the sake of simplicity, some components are not shown.
The air purification apparatus 1 of the present embodiment includes a plurality (four in the illustrated example) of gas-liquid contact portions 5a to 5d and a plurality of pairs (four in the illustrated example) of the injection nozzles 6a to 6d, 7a to 7d, which are accommodated in a plurality (two in the illustrated example) of the casings 2a and 2b. Specifically, one gas-liquid contact portion 5a and a pair of jet nozzles 6a and 7a are accommodated in the first housing 2a, and the three gas-liquid contact portions 5b to 5d are accommodated in the second housing 2b. And three pairs of injection nozzles 6b to 6d and 7b to 7d.
 2つの筐体2a,2bは、第1の筐体2aの排気口4aと第2の筐体2bの吸気口3bとが管路などにより直列に接続され、第1の筐体2aから排出された空気が第2の筐体2bに導入されるようになっている。加えて、第2の筐体2bに収容された3つの気液接触部5b~5dは、空気の流れ方向に沿って一列に配置されている。これにより、本実施形態の空気浄化装置1では、被処理空気の多段処理(直列処理)が可能となり、微粒子やガス状物質の除去性能をさらに向上させることができる。また、被処理空気の種類、汚染度(空気中に含まれる汚染物質の濃度や粒子径など)、温度、湿度、蒸気圧、風量、風速や圧力に応じて、気液接触部5a~5dごとに構成(例えば、繊維集合体を構成する繊維の比表面積など)を変更したり、噴射する洗浄水の種類を変更したりすることで、微粒子やガス状物質をより効果的に除去することも可能になる。
 なお、洗浄水を循環させる循環ポンプは、筐体2a,2bごとに1つずつ設けられていてもよく、第2の筐体2bにのみ設けられていてもよい。また、第2の筐体2bには、複数の循環ポンプが設けられ、例えば気液接触部5b~5dごとに洗浄水を循環させるようになっていてもよい。さらに、第2の筐体2bの循環タンク8bは、気液接触部5b~5dの数に応じて、板状部材、スリット入り板材、フィルタ、半透膜などの仕切りによって、複数の小タンクに分割されていてもよい。その場合、例えば、洗浄水が下流側から上流側へ高低差で流れるように、小タンク同士の間に段差が設けられていてもよい。仕切りとしてフィルタを用いる場合には、各フィルタの孔径が、下流側に向かうにつれて徐々に小さくなっていてもよい。
In the two casings 2a and 2b, the exhaust port 4a of the first casing 2a and the intake port 3b of the second casing 2b are connected in series by a pipe or the like, and are discharged from the first casing 2a. The air is introduced into the second housing 2b. In addition, the three gas-liquid contact portions 5b to 5d accommodated in the second casing 2b are arranged in a line along the air flow direction. Thereby, in the air purification apparatus 1 of this embodiment, the multi stage process (serial process) of to-be-processed air is attained, and the removal performance of a particulate matter or a gaseous substance can further be improved. In addition, depending on the type of air to be treated, the degree of contamination (concentration and particle diameter of pollutants contained in the air), temperature, humidity, vapor pressure, air volume, wind speed and pressure, the gas-liquid contact parts 5a to 5d It is also possible to more effectively remove fine particles and gaseous substances by changing the configuration (for example, the specific surface area of the fibers constituting the fiber assembly) or changing the type of washing water to be injected. It becomes possible.
One circulation pump for circulating the cleaning water may be provided for each of the casings 2a and 2b, or may be provided only for the second casing 2b. Further, the second casing 2b may be provided with a plurality of circulation pumps, for example, to circulate cleaning water for each of the gas-liquid contact portions 5b to 5d. Furthermore, the circulation tank 8b of the second housing 2b is divided into a plurality of small tanks by partitioning a plate-shaped member, a slit-containing plate material, a filter, a semipermeable membrane or the like according to the number of gas-liquid contact portions 5b to 5d. It may be divided. In that case, for example, a step may be provided between the small tanks so that the washing water flows with a height difference from the downstream side to the upstream side. When using a filter as a partition, the hole diameter of each filter may become small gradually as it goes downstream.
 本実施形態では、複数の気液接触部5a~5dが、空気流路に沿って一列に配置されているが、気液接触部は、空気流路と交差する方向に一列に配置されていてもよい。これにより、被処理空気の並列処理が可能となり、処理風量の増大にも対応することができる。あるいは、除去性能と処理風量とを共に向上させるために、気液接触部は、水平面内で2方向に積層されて2次元的に配置されていてもよく、垂直方向にも積層されて3次元的に配置されていてもよい。なお、気液接触部が2次元的または3次元的に配置されている場合、空気の流れは一方向でなくてもよく、筐体内を折り返して流れるようになっていてもよい。
 次に、具体的な実施例を挙げて、本発明をより詳細に説明する。
In the present embodiment, the plurality of gas-liquid contact portions 5a to 5d are arranged in a line along the air flow path, but the gas-liquid contact parts are arranged in a line in a direction intersecting the air flow path. Also good. Thereby, parallel processing of air to be processed is possible, and it is possible to cope with an increase in the processing air volume. Alternatively, in order to improve both the removal performance and the processing air volume, the gas-liquid contact portions may be two-dimensionally stacked in two directions in a horizontal plane, or three-dimensionally stacked in the vertical direction. May be arranged. In addition, when the gas-liquid contact part is arrange | positioned two-dimensionally or three-dimensionally, the flow of air does not need to be one direction, and it may flow in the housing | casing.
Next, the present invention will be described in more detail with reference to specific examples.
 (実施例1)
 本実施例では、第1の実施形態の空気浄化装置を用いて、空気浄化処理によるメタノール除去率(メタノールガスの濃度変化)を測定した。なお、本実施例で用いた空気浄化装置には、水返し部および繊維シートは設けられていない。
 筐体として、幅が170mm、高さが300mm、奥行きが350mmの内部空間を形成するものを用い、気液接触部として、厚みが20mm、幅が170mm、繊維の繊度が75デニール、比表面積が890m/mのサランロック(品番:CS-120)を使用し、前面と水平面との角度を90°とした。また、エリミネータとして、繊維の繊度が75デニール、厚みが20mm、幅が170mm、比表面積が890m/mのサランロック(品番:CS-120)を使用した。
Example 1
In this example, the methanol removal rate (change in the concentration of methanol gas) by the air purification process was measured using the air purification apparatus of the first embodiment. In addition, the water purifier and the fiber sheet are not provided in the air purifier used in the present Example.
As the casing, a housing that forms an internal space with a width of 170 mm, a height of 300 mm, and a depth of 350 mm is used. As the gas-liquid contact portion, the thickness is 20 mm, the width is 170 mm, the fiber fineness is 75 denier, and the specific surface area is An 890 m 2 / m 3 Saran lock (product number: CS-120) was used, and the angle between the front surface and the horizontal plane was 90 °. As an eliminator, Saran lock (product number: CS-120) having a fiber fineness of 75 denier, a thickness of 20 mm, a width of 170 mm, and a specific surface area of 890 m 2 / m 3 was used.
 噴射ノズルとして、株式会社いけうち製の広角扇形ノズル(形番:1/8MYYP030PVC)を用い、筐体の幅方向の中央に1つずつ配置した。噴射ノズルからの洗浄水の噴射方向は垂直方向上方とし、噴射流量は3L/minとした。
 気液接触部に流入させる被処理空気として、インピンジャーによってガス濃度が400ppmに調節されたメタノールガスを用い、処理風量は36m/hとした。メタノール除去率は、吸気口の上流側および排気口の下流側にそれぞれ設けられた検知管により、被処理空気のメタノール濃度と浄化された空気のメタノール濃度とから算出した。また、差圧は、差圧計により、吸気口の上流側と排気口の下流側との圧力差として測定した。
A wide-angle fan-shaped nozzle (model number: 1/8 MYP030PVC) manufactured by Ikeuchi Co., Ltd. was used as the spray nozzle, and one nozzle was arranged at the center in the width direction of the housing. The direction of spraying the washing water from the spray nozzle was set vertically upward and the spray flow rate was 3 L / min.
As the air to be treated flowing into the gas-liquid contact portion, methanol gas whose gas concentration was adjusted to 400 ppm by an impinger was used, and the treatment air flow rate was 36 m 3 / h. The methanol removal rate was calculated from the methanol concentration of the air to be treated and the methanol concentration of the purified air by the detection tubes provided on the upstream side of the intake port and the downstream side of the exhaust port, respectively. The differential pressure was measured as a pressure difference between the upstream side of the intake port and the downstream side of the exhaust port using a differential pressure gauge.
 (実施例2)
 繊維集合体の前面と水平面との角度を80°にした以外、実施例1と同様の条件でメタノール除去率を測定した。
(Example 2)
The methanol removal rate was measured under the same conditions as in Example 1 except that the angle between the front surface of the fiber assembly and the horizontal plane was 80 °.
 (比較例1)
 噴射ノズルとして、株式会社いけうち製の充円錐ノズル(形番:1/8MINJJX030PP(FEPM)+PPS)を用い、気液接触部の前方および後方にそれぞれ配置した以外、実施例1と同様の条件でメタノール除去率を測定した。
(Comparative Example 1)
Methanol is used under the same conditions as in Example 1 except that a full cone nozzle (model number: 1/8 MINJJX030PP (FEPM) + PPS) manufactured by Ikeuchi Co., Ltd. is used as the injection nozzle and is arranged in front and rear of the gas-liquid contact portion. The removal rate was measured.
 (比較例2)
 繊維集合体の前面と水平面との角度を80°にした以外、比較例1と同様の条件でメタノール除去率を測定した。
 表1に、実施例1、実施例2、比較例1、および比較例2における、メタノール除去率および差圧の結果を示す。
(Comparative Example 2)
The methanol removal rate was measured under the same conditions as in Comparative Example 1 except that the angle between the front surface of the fiber assembly and the horizontal plane was 80 °.
Table 1 shows the results of methanol removal rate and differential pressure in Example 1, Example 2, Comparative Example 1, and Comparative Example 2.
Figure JPOXMLDOC01-appb-T000001
Figure JPOXMLDOC01-appb-T000001
  実施例1および実施例2では、比較例1および比較例2と比べて、メタノール除去率および差圧の両方で良好な結果が得られていることが確認された。これは、洗浄水の噴射形態の違いによるものであり、気液接触部に対して下方から平面状に洗浄水を噴射したことによる効果であると考えられる。一方で、実施例1と実施例2を比較すると、メタノール除去率の点で実施例2がより良好であるが、これは、気液接触部を空気の流れ方向に対して上流側に前傾させた効果であると考えられる。 In Example 1 and Example 2, compared to Comparative Example 1 and Comparative Example 2, it was confirmed that good results were obtained in both methanol removal rate and differential pressure. This is due to the difference in the jet form of the wash water, and is considered to be the effect of jetting the wash water from the bottom to the gas-liquid contact portion from below. On the other hand, when Example 1 and Example 2 are compared, Example 2 is better in terms of the methanol removal rate. This is because the gas-liquid contact portion is inclined forward with respect to the air flow direction. This is considered to be the effect.
 1 空気浄化装置
 2 筐体
 3 吸気口
 4 排気口
 5,5a~5d 気液接触部
 6,6a~6d 前面噴射ノズル(洗浄水噴射手段)
 7,7a~7d 背面噴射ノズル(他の洗浄水噴射手段)
 8 循環タンク
 9 循環ポンプ
 10 外部水源
 11~13 配管
 14 給水弁
 15 排水弁
 16 エリミネータ
 17 送風機
 18 水返し部
 19 繊維シート
 21 供給流路
 22 噴射流路
 22a 噴射開口
 23 傾斜案内面
DESCRIPTION OF SYMBOLS 1 Air purification apparatus 2 Housing | casing 3 Intake port 4 Exhaust port 5,5a-5d Gas- liquid contact part 6,6a-6d Front injection nozzle (washing water injection means)
7, 7a-7d Back spray nozzle (other cleaning water spray means)
DESCRIPTION OF SYMBOLS 8 Circulation tank 9 Circulation pump 10 External water source 11-13 Pipe 14 Water supply valve 15 Drain valve 16 Eliminator 17 Blower 18 Water return part 19 Fiber sheet 21 Supply flow path 22 Injection flow path 22a Injection opening 23 Inclination guide surface

Claims (10)

  1.  筐体の内部を空気が水平方向に流れるように該筐体に設けられた吸気口および排気口と、
     前記吸気口と前記排気口との間に設けられ、前記吸気口から前記筐体内に導入された空気を洗浄水と接触させる気液接触部と、
     空気の流れ方向に対して前記気液接触部の上流側に設けられ、下方から上方に向けて前記流れ方向と交差する方向に前記洗浄水を平面状に噴射する洗浄水噴射手段と、
     を有する空気浄化装置。
    An intake port and an exhaust port provided in the housing so that air flows horizontally in the housing;
    A gas-liquid contact portion that is provided between the intake port and the exhaust port, and that makes air introduced into the housing from the intake port come into contact with cleaning water;
    Wash water injection means that is provided on the upstream side of the gas-liquid contact portion with respect to the air flow direction, and that jets the wash water in a plane that intersects the flow direction from below to above,
    An air purifying device.
  2.  前記気液接触部は、上部が下部よりも前記流れ方向の上流側に位置するように傾斜した傾斜面を有する、請求項1に記載の空気浄化装置。 The air purification device according to claim 1, wherein the gas-liquid contact portion has an inclined surface that is inclined such that an upper portion is located upstream of the lower portion in the flow direction.
  3.  前記流れ方向に対して前記気液接触部の下流側に設けられ、下方から上方に向けて前記流れ方向と交差する方向に前記洗浄水を平面状に噴射する他の洗浄水噴射手段を有する、請求項1または2に記載の空気浄化装置。 Other cleaning water jetting means is provided on the downstream side of the gas-liquid contact portion with respect to the flow direction, and jets the wash water in a direction crossing the flow direction from below to above. The air purification apparatus according to claim 1 or 2.
  4.  前記洗浄水噴射手段と前記他の洗浄水噴射手段が、それぞれ異なる種類の前記洗浄水を噴射する、請求項3に記載の空気浄化装置。 The air purifier according to claim 3, wherein the cleaning water spraying unit and the other cleaning water spraying unit spray different types of the cleaning water.
  5.  前記洗浄水噴射手段は、前記筺体内を流れる空気の流速または流量に応じて前記洗浄水の噴射方向が変更可能である、請求項1から4のいずれか1項に記載の空気浄化装置。 The air purification device according to any one of claims 1 to 4, wherein the washing water jetting unit is capable of changing a jetting direction of the washing water according to a flow rate or a flow rate of air flowing through the housing.
  6.  前記流れ方向に対して前記洗浄水噴射手段の上流側で、前記筐体の内側上面から下方に突出する水返し部を有する、請求項1から5のいずれか1項に記載の空気浄化装置。 The air purification device according to any one of claims 1 to 5, further comprising a water return portion that protrudes downward from an inner upper surface of the housing on the upstream side of the washing water injection unit with respect to the flow direction.
  7.  前記水返し部の先端から垂れ下がる繊維シートを有する、請求項6に記載の空気浄化装置。 The air purification apparatus according to claim 6, further comprising a fiber sheet hanging from the tip of the water return portion.
  8.  前記洗浄水噴射手段が、開口部を有するパイプと、前記開口部に接続され、前記洗浄水を扇形状に噴射するノズルと、を有する、請求項1から7のいずれか1項に記載の空気浄化装置。 The air according to any one of claims 1 to 7, wherein the cleaning water injection unit includes a pipe having an opening and a nozzle that is connected to the opening and injects the cleaning water into a fan shape. Purification equipment.
  9.  前記ノズルは、前記パイプに連通する供給流路と、前記供給流路に連通し、前記供給流路の径よりも小さい径を有する噴射流路と、前記噴射流路の噴射開口に対向する位置に設けられ、前記噴射流路の軸線に対して傾斜した傾斜案内面であって、前記噴射開口から噴射された洗浄水を該傾斜案内面に沿って外部に案内することで、前記洗浄水を平面状に噴射させる傾斜案内面と、を有する、請求項8に記載の空気浄化装置。 The nozzle communicates with the pipe, a supply channel that communicates with the supply channel, an injection channel that has a diameter smaller than the diameter of the supply channel, and a position facing the injection opening of the injection channel An inclined guide surface that is inclined with respect to the axis of the injection flow path and guides the wash water ejected from the injection opening to the outside along the inclined guide surface, thereby The air purification device according to claim 8, further comprising an inclined guide surface that is jetted in a planar shape.
  10.  複数の前記気液接触部が、水平方向および垂直方向の少なくとも一方に沿って積層されている、請求項1から9のいずれか1項に記載の空気浄化装置。 The air purification device according to any one of claims 1 to 9, wherein the plurality of gas-liquid contact portions are stacked along at least one of a horizontal direction and a vertical direction.
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