WO2020145345A1 - Air filter - Google Patents
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- WO2020145345A1 WO2020145345A1 PCT/JP2020/000446 JP2020000446W WO2020145345A1 WO 2020145345 A1 WO2020145345 A1 WO 2020145345A1 JP 2020000446 W JP2020000446 W JP 2020000446W WO 2020145345 A1 WO2020145345 A1 WO 2020145345A1
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- filler
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation 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
- B01D53/02—Separation 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 adsorption, e.g. preparative gas chromatography
- B01D53/04—Separation 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 adsorption, e.g. preparative gas chromatography with stationary adsorbents
- B01D53/0407—Constructional details of adsorbing systems
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- A—HUMAN NECESSITIES
- A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
- A61L—METHODS 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
- A61L9/00—Disinfection, sterilisation or deodorisation of air
- A61L9/01—Deodorant compositions
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- A—HUMAN NECESSITIES
- A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
- A61L—METHODS 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
- A61L9/00—Disinfection, sterilisation or deodorisation of air
- A61L9/01—Deodorant compositions
- A61L9/014—Deodorant compositions containing sorbent material, e.g. activated carbon
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D46/00—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D46/00—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours
- B01D46/0027—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours with additional separating or treating functions
- B01D46/0036—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours with additional separating or treating functions by adsorption or absorption
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D46/00—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours
- B01D46/24—Particle separators, e.g. dust precipitators, using rigid hollow filter bodies
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D46/00—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours
- B01D46/24—Particle separators, e.g. dust precipitators, using rigid hollow filter bodies
- B01D46/2403—Particle separators, e.g. dust precipitators, using rigid hollow filter bodies characterised by the physical shape or structure of the filtering element
- B01D46/2418—Honeycomb filters
- B01D46/2425—Honeycomb filters characterized by parameters related to the physical properties of the honeycomb structure material
- B01D46/2429—Honeycomb filters characterized by parameters related to the physical properties of the honeycomb structure material of the honeycomb walls or cells
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D46/00—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours
- B01D46/24—Particle separators, e.g. dust precipitators, using rigid hollow filter bodies
- B01D46/2403—Particle separators, e.g. dust precipitators, using rigid hollow filter bodies characterised by the physical shape or structure of the filtering element
- B01D46/2418—Honeycomb filters
- B01D46/2451—Honeycomb filters characterized by the geometrical structure, shape, pattern or configuration or parameters related to the geometry of the structure
- B01D46/248—Structures comprising laminated bodies or discs
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D46/00—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours
- B01D46/24—Particle separators, e.g. dust precipitators, using rigid hollow filter bodies
- B01D46/2403—Particle separators, e.g. dust precipitators, using rigid hollow filter bodies characterised by the physical shape or structure of the filtering element
- B01D46/2418—Honeycomb filters
- B01D46/2451—Honeycomb filters characterized by the geometrical structure, shape, pattern or configuration or parameters related to the geometry of the structure
- B01D46/2482—Thickness, height, width, length or diameter
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation 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
- B01D53/02—Separation 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 adsorption, e.g. preparative gas chromatography
- B01D53/04—Separation 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 adsorption, e.g. preparative gas chromatography with stationary adsorbents
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
- B01J20/02—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material
- B01J20/20—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material comprising free carbon; comprising carbon obtained by carbonising processes
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2253/00—Adsorbents used in seperation treatment of gases and vapours
- B01D2253/10—Inorganic adsorbents
- B01D2253/102—Carbon
Definitions
- the present invention relates to an air filter used for purposes such as deodorization.
- the present application claims priority on the basis of application number 201910020245.3, filed with the China Intellectual Property Office on January 9, 2019, the content of which is incorporated herein by reference.
- a corrugated honeycomb structure having a large number of cells is known by alternately stacking a plurality of liner members and a plurality of corrugated members. ..
- the air to be treated is purified by the malodorous components and the like adsorbing to the corrugated honeycomb structure while passing through the cells.
- a material for the corrugated honeycomb structure paper to which an adsorbent is attached or contained is usually used.
- a deodorizing filter in which cells of a corrugated honeycomb structure are filled with activated carbon or the like has also been proposed for the purpose of improving adsorption efficiency and sustainability (Patent Document 1).
- the present invention has been made in view of the above circumstances, and provides an air filter having enhanced adsorption efficiency and sustainability by being filled with a filler such as activated carbon while suppressing an increase in pressure loss. Is an issue.
- a planar air filter having a first surface and a second surface, A corrugated honeycomb structure that defines a plurality of cells arranged in the surface direction, and a plurality of porous fillers filled in the plurality of cells,
- the plurality of cells comprises a plurality of smallest diameter cells and a plurality of large diameter cells,
- the plurality of smallest diameter cells are cells having the smallest diameter of the inscribed circle,
- the plurality of large-diameter cells is a cell in which the diameter of the inscribed circle is larger than the diameter of the inscribed circle of the plurality of smallest-diameter cells,
- the ratio of the number of the minimum diameter cells filled with the filler to the number of the minimum diameter cells is 50% or less,
- the air filter wherein the ratio of the number of the large-sized cells filled with the filler in the number of the large-sized cells is 25 to 100%.
- the corrugated honeycomb structure is configured by bonding a plurality of liner members and a plurality of corrugated members to each other, The plurality of liner members are linear when observed from a direction perpendicular to the surface direction, The plurality of corrugated members has a corrugated shape in which peaks and valleys are repeated along the direction in which the liner member extends when observed from a direction perpendicular to the surface direction,
- the air filter of the present invention filled with a filler such as activated carbon, it is possible to enhance adsorption efficiency and sustainability while suppressing an increase in pressure loss.
- the air filter of the present invention comprises a corrugated honeycomb structure defining a plurality of cells arranged in the plane direction, and a plurality of porous fillers filled in the plurality of cells.
- FIG. 1 is a view of a corrugated honeycomb structure 1 used for an air filter according to an embodiment of the present invention as seen from a direction perpendicular to a plane direction.
- the corrugated honeycomb structure 1 is composed of a liner member 10 and a corrugated member 20, and is a planar body in which the front side of the paper surface in FIG. 1 is a first surface 61 and the back side of the paper surface is a second surface 62.
- the thickness of the corrugated honeycomb structure (the length in the depth direction of the cells of the corrugated honeycomb structure, which will be described later) may be adjusted in the range of 5 to 100 mm, and usually 5 to 50 mm.
- the liner member 10 looks like a straight line or a substantially straight line when observed from a direction perpendicular to the surface direction, and is a strip-shaped member having a width in the thickness direction of the paper surface of FIG.
- the corrugated member 20 has a corrugated shape in which a strip-shaped member is repeatedly bent, and peaks and valleys are repeated along the direction in which the liner member 10 extends when observed from a direction perpendicular to the plane direction. It is a shaped member.
- two kinds of corrugated members 20, a small corrugated member 21 and a large corrugated member 22, are used.
- the pitch and height of the large corrugated member 22 are larger than the pitch and height of the small corrugated member 21.
- the valley portion 21b of the small corrugated member 21 is bonded to one liner member 10, and the peak portion 21a is bonded to another liner member 10.
- the valley portion 22b of the large corrugated member 22 is bonded to the one liner member 10, but the crest portion 22a does not involve the other one liner member 10 and the other large corrugated member 22. Is directly bonded to the mountain portion 22a.
- a plurality of cells 30 defined by the liner member 10 and the corrugated member 20 are formed so as to be arranged in the plane direction.
- a minimum diameter cell 31 and two types of large diameter cells are formed as the cell 30, a minimum diameter cell 31 and two types of large diameter cells (first large diameter cell 32 and second large diameter cell 33) are formed.
- the smallest diameter cell 31 is a space defined by the liner member 10 and the small corrugated member 21.
- the first large-diameter cell 32 is a space defined by the liner member 10 and the large corrugated member 22.
- the second large-diameter cell 33 is a space defined by the pair of large corrugated members 22 to which the mountain portions 22a are directly adhered.
- a minimum diameter inscribed circle 41 is an inscribed circle of the minimum diameter cell 31
- a first large diameter inscribed circle 42 is an inscribed circle of the first large diameter cell 32
- a second large diameter inscribed circle is an inscribed circle of the second large diameter cell 33.
- the smallest diameter inscribed circle 41 has the smallest diameter
- the diameters of the first large diameter inscribed circle 42 and the second large diameter inscribed circle 43 are smaller than the diameter of the smallest diameter inscribed circle 41. large.
- the diameter of the second large-diameter inscribed circle 43 is larger than the diameter of the first large-diameter inscribed circle 42.
- the smallest-diameter cell 31 inscribed by the smallest-diameter inscribed circle 41 has a small opening area, so it is difficult for the filler to be filled and the gas can smoothly pass through. Further, since the opening area of the smallest diameter cell 31 is small, the gas passing through the smallest diameter cell 31 can sufficiently contact the liner member 10 and the small corrugated member 21, and the malodorous components and the like are adsorbed on these members. Cheap.
- first large-diameter cell 32 and the second large-diameter cell 33 which are inscribed by an inscribed circle having a diameter larger than the minimum-diameter inscribed circle 41, have a sufficient size so that the minimum-diameter cell 31 is difficult to enter. Can be filled. Therefore, it is possible to enhance the adsorption efficiency and sustainability by the filler while suppressing the increase in pressure loss.
- first large-diameter cell 32, second large-diameter cell 33 having different inscribed circle diameters, the effect of suppressing an increase in pressure loss can be obtained.
- the ratio of the total area of the smallest diameter cells 31 to the total area (100%) of the cells 30 in the corrugated honeycomb structure 1 (the proportion (area %) of the smallest diameter cells 31 in the plurality of cells 30 of the corrugated honeycomb structure 1) is preferably 10 to 90%, more preferably 15 to 75%, and further preferably 20 to 50%.
- the ratio is equal to or higher than the preferable lower limit value, it is easy to secure air permeability and suppress an increase in pressure loss.
- the ratio is equal to or less than the preferable upper limit value, it is easy to fill the first large diameter cell 32 and the second large diameter cell 33 with a sufficient amount of the filler.
- the total area of the first large-diameter cell 32 and the total area of the second large-diameter cell 33 may be appropriately adjusted according to the blending amount for each size of the filler to be filled.
- the smallest diameter cells 31, the first large diameter cells 32, and the second large diameter cells 33 are distributed as evenly as possible in the direction in which the liner members 10 are arranged. This can prevent a partial increase in pressure loss.
- the diameter of the smallest diameter inscribed circle 41 is preferably 0.5 to 3 mm, more preferably 1 to 2.5 mm, and further preferably 1.5 to 2.0 mm.
- the diameter of the smallest diameter inscribed circle 41 is equal to or larger than the lower limit value of the preferable range, it is difficult to prevent gas from passing through the smallest diameter cell 31. If the diameter of the smallest diameter inscribed circle 41 is equal to or less than the upper limit value of the preferable range, the gas passing through the smallest diameter cell 31 is sufficiently brought into contact with the corrugated honeycomb structure 1 so that the malodorous components and the like are transferred to the corrugated honeycomb structure 1. Can be adsorbed.
- the diameters of the first large diameter inscribed circle 42 and the second large diameter inscribed circle 43 are preferably 1.1 times or more, and preferably 1.5 times or more, the diameter of the smallest diameter inscribed circle 41. More preferable. When the ratio is equal to or more than the preferable ratio, it is easy to fill the first large diameter cell 32 and the second large diameter cell 33 with the filler while suppressing the filling of the smallest diameter cell 31 with the filler.
- the diameter of the first large diameter inscribed circle 42 is preferably 1 to 6 mm, more preferably 1 to 4 mm, and further preferably 2 to 3 mm.
- the diameter of the first large-diameter inscribed circle 42 is equal to or larger than the lower limit value of the preferable range, it is easy to fill the first large-diameter cell 32 with the filler. If the diameter of the first large-diameter inscribed circle 42 is equal to or smaller than the upper limit of the preferable range, the area of the first large-diameter cell 32 does not become excessively large, and the strength of the corrugated honeycomb structure 1 can be easily ensured.
- the diameter of the second large diameter inscribed circle 43 is preferably 1.1 times or more, and more preferably 1.25 times or more the diameter of the first large diameter inscribed circle 42.
- the ratio is equal to or more than the above preferable ratio, it is easy to fill the fillers of different sizes by using the first large diameter cell 32 and the second large diameter cell 33.
- the pitch and height of the corrugated shape of the small corrugated member 21 can be determined so that the diameter of the smallest diameter inscribed circle 41 has the above-described preferable value.
- the pitch of the corrugated shape of the small corrugated member 21 is preferably 2 to 7 mm, more preferably 3 to 6 mm.
- the corrugated height of the small corrugated member 21 is preferably 0.5 to 3 mm, more preferably 1 to 2.5 mm.
- the corrugated height of the small corrugated member 21 is the distance in the height direction between the valleys 21b and the ridges 21a on one surface of the small corrugated member 21, and the height direction means the liner member 10. It is a direction orthogonal to each other.
- the pitch and height of the corrugated shape of the large corrugated member 22 can be determined so that the diameters of the first large diameter inscribed circle 42 and the second large diameter inscribed circle 43 are the above-mentioned preferable values.
- the corrugated pitch of the large corrugated member 22 is preferably 4 to 12 mm, and more preferably 5 to 10 mm.
- the corrugated height of the large corrugated member 22 is preferably 2 to 6 mm, more preferably 2.5 to 5 mm.
- the corrugated height of the large corrugated member 22 is the distance in the height direction between the valleys 22b and the ridges 22a on one surface of the large corrugated member 22, and the height direction means the liner member 10. It is a direction orthogonal to each other.
- the liner member 10 and the corrugated member 20 of the corrugated honeycomb structure 1 are preferably composed of a base material and an adsorbent held by the base material.
- the base material is not particularly limited as long as it is a sheet-shaped base material such as papers, non-woven fabrics and plastic films, but a fiber base material is preferable from the viewpoint of easily holding the adsorbent.
- the fiber substrate include a paper substrate containing cellulose fiber as a main component and a plastic substrate containing synthetic fiber as a main component. Of these, a paper base material containing cellulose fibers as a main component is preferable.
- "to be a main component" means that the ratio to the whole base material is 50% by mass or more.
- the paper base material is typically composed of pulp containing cellulose fibers.
- pulp containing cellulose fibers include wood pulp and non-wood pulp.
- wood pulp include softwood pulp and hardwood pulp.
- non-wood pulp include hemp pulp, kenaf pulp, bamboo pulp and the like.
- the wood pulp may have been subjected to a cooking process and/or a bleaching process.
- wood pulp is used after being subjected to various cooking and bleaching steps in order to remove components other than cellulose from the raw material wood.
- the cooking step and the bleaching step are not particularly limited, and a known method can be appropriately used. These pulps may be used alone or in combination of two or more.
- the paper substrate may further contain fibers other than cellulose fibers.
- fibers include rayon fibers, polyethylene fibers, polypropylene fibers, polyester fibers and other synthetic fibers, glass fibers, ceramic fibers, mineral fibers and other inorganic fibers, and animal fibers.
- the paper base material may contain internal additives such as a sizing agent, a paper strengthening agent, a coloring agent, a preservative, and a flame retardant. Known internal additives can be used.
- plastic substrate examples include those containing, as a main component, one or more kinds of synthetic fibers such as rayon fiber, polyethylene fiber, polypropylene fiber and polyester fiber.
- the basis weight of the base material is preferably 10 to 500 g/m 2 , more preferably 10 to 400 g/m 2 , and even more preferably 10 to 300 g/m 2 .
- the fiber base material is preferably obtained by a papermaking method.
- Examples of the adsorbent to be held on the base material include known adsorbents such as granular, powdery, fibrous and the like activated carbon, mordenite, ferrierite, molecular sieves and other zeolites, silica gel and alumina gel.
- a chemical that reacts with the component to be removed (for example, a compound that reacts with ammonia or formaldehyde) may be carried on these adsorbents.
- a chemical that reacts with the component to be removed may be directly supported on the base material.
- the adsorbent to be held on the base material may be held inside the base material, adhered to the surface, or present both inside and on the surface.
- the adsorbent to be held on the substrate may be added internally during paper making, or may be applied or impregnated after paper making.
- the method of manufacturing the corrugated honeycomb structure 1 is not particularly limited, but a single corrugated cardboard in which the small corrugated member 21 is bonded to the liner member 10 (hereinafter referred to as “small corrugated cardboard”) and a large corrugated member 22 in the liner member 10 are bonded. It is preferable that the single-sided corrugated board (hereinafter referred to as “large-sized corrugated board”) thus laminated is laminated and bonded.
- the mountain portions 22a of the pair of large corrugated members 22 are bonded to each other, the pair of large corrugated members 22 are bonded between the pair of liner members 10, and the mountain portions 22a of the pair of large corrugated members 22 are bonded to each other.
- X structure flute the structure sandwiched in this state
- the X structure flute 70 in FIG. 2 is laminated and adhered to the X structure flute 70 and the small piece corrugated board.
- the liner member 10 of the X structure flute 70 and the liner member 10 of the small piece corrugated board may be overlapped. Further, the small corrugated cardboard on the side of the small corrugated member 21 is adhered to the liner member 10 of the X structure flute 70, and the liner member 10 of the small corrugated cardboard and the liner member 10 of other small corrugated cardboard are overlapped and laminated and bonded. Good.
- the corrugated honeycomb structure 1 is manufactured by laminating and adhering the small piece corrugated board and the X-structure flute, the part where the liner member 10 that constitutes one piece corrugated board is present independently and the two pieces that form a pair of piece corrugated board. And a portion of the liner member 10 existing in a state of being overlapped with each other.
- FIG. 3 is a schematic sectional view of an air filter according to an embodiment of the present invention.
- the cells 30 of the corrugated honeycomb structure 1 shown in FIGS. 1 and 2 are filled with a plurality of porous fillers 50, and the first surface 61 and the second surface of the corrugated honeycomb structure 1 are formed.
- a breathable sheet 71 and a breathable sheet 72 are arranged respectively.
- the filler 50 Since the filler 50 is porous, it has the ability to adsorb removed components such as malodors.
- the filler 50 include granular, powder and fibrous activated carbon, mordenite, ferrierite, zeolite such as molecular sieves, silica gel and alumina gel. Among them, activated carbon is preferable, granular activated carbon is more preferable, and spherical or substantially spherical activated carbon is particularly preferable.
- the filler 50 may carry a chemical that reacts with a component to be removed such as an inorganic acid.
- the filler 50 is preferably granular, more preferably substantially spherical, and particularly preferably spherical. If the cells 30 are spherical or substantially spherical, the cells 30 can be easily filled, and an appropriate gap is created between the cells 30 and the liner member 10 or the corrugated member 20 that defines the cells 30, so that ventilation can be easily ensured.
- the average particle size of the filler 50 is preferably 500 to 10000 ⁇ m, more preferably 1000 to 5000 ⁇ m.
- the average particle diameter is measured by the mass average particle diameter method according to JIS K1474 (Activated carbon test method-Average particle diameter measurement method).
- the specific surface area of the filler 50 is preferably 600 to 2200 m 2 /g.
- the specific surface area is the BET specific surface area measured by the nitrogen gas adsorption method.
- the specific surface area of the filler 50 is equal to or more than the preferable lower limit value, it is easy to exhibit the adsorption performance of the malodorous component and the like.
- the specific surface area of the filler 50 is equal to or less than the preferable upper limit value, the strength of the filler 50 is easily maintained.
- the ratio (filling rate) of the number of the smallest diameter cells 31 filled with the filler 50 to the number (100%) of the smallest diameter cells 31 is preferably 50% or less, and more preferably 25% or less. It is preferably 10% or less, and more preferably 10% or less. If the filling rate of the smallest diameter cells 31 is equal to or lower than the preferable upper limit value, it is easy to ensure air permeability. In order to set the filling rate of the smallest diameter cell 31 to be equal to or less than the preferable upper limit value, the proportion of the filler 50 having a diameter smaller than that of the smallest diameter inscribed circle 41 to the entire filler 50 may be lowered. The lower limit of the filling rate of the smallest diameter cells 31 may be 0%. That is, the minimum diameter cell 31 may not be filled with the filler 50.
- the ratio of the number of large-diameter cells filled with the filler 50 to the number (100%) of the large-diameter cells (the first large-diameter cell 32 and the second large-diameter cell 33 in this embodiment) (filling ratio) ) Is preferably 25 to 100%, more preferably 50 to 100%, and further preferably 75 to 100%.
- the filling rate of the large-diameter cell is equal to or higher than the preferable lower limit value, it is easy to increase the adsorption efficiency and sustainability by the filler 50. If the filling rate of the large-diameter cell is equal to or less than the preferable upper limit value, the filling operation is easy. In determining the filling rate, cells filled with at least one filling agent are treated as filled cells regardless of the size of the filling agent 50.
- FIG. 3 schematically shows an example in which a spherical small filler 51 and a large filler 52 larger than the small filler 51 are filled as the filler 50.
- the diameter of the small filler 51 is preferably larger than the minimum diameter inscribed circle 41. As a result, the small filler 51 is less likely to be filled in the smallest diameter cell 31. Even if the diameter of the filler 50 is larger than the smallest diameter inscribed circle 41, the smallest diameter cell 31 may be filled with the filler 50 or the like that is broken due to cracking or the like.
- each diameter is smaller than the second large diameter inscribed circle 43. Further, the diameter of the large filler 52 is preferably larger than the first large diameter inscribed circle 42. Thereby, the large filler 52 is easily filled in the second large-diameter cell 33, and the filling rate of the second large-diameter cell 33 can be improved.
- the breathable sheet 71 and the breathable sheet 72 are made of a breathable material such as nonwoven fabric or mesh cloth. Examples of the material forming the non-woven fabric, the mesh cloth and the like include rayon, polyester, nylon and the like.
- the breathable sheet 71 and the breathable sheet 72 are arranged by being bonded to the first surface 61 value and the second surface 62 of the corrugated honeycomb structure 1, respectively. By positioning the breathable sheet 71 and the breathable sheet 72, it is possible to prevent the filler 50 from falling off from the air filter. Further, dust or the like can be removed from the gas passing through the air filter.
- the corrugated honeycomb structure 1 having the X-structured flutes 70 is shown in FIGS. 1 and 2, it is not always necessary to have the X-structured flutes 70.
- three types of single-faced corrugated boards having different sizes may be used in combination and laminated.
- the large-diameter cell is not limited to two types as shown in FIGS. 1 and 2, and may be one type or three or more types.
- the shape of the cell 30 is not particularly limited.
- the large corrugated member 22 and the small corrugated member 21 are different in both pitch and height, but a plurality of types of corrugated members 20 different in only one of pitch and height are used. Good.
- the corrugated member 20 may be of one type as long as the cells 30 can include cells of different sizes.
- a plurality of X-structure flutes made by using one type of corrugated cardboard may be laminated.
- the shape and size of the filler 50 are not limited to two types as shown in FIG. 3, and may be three or more types.
- Example 1 A glass fiber mixed paper (manufactured by Oji Ftex Co., Ltd.) having a basis weight of 50 g/m 2 is used as a liner base paper, and an adsorbent dispersion liquid containing activated carbon, an inorganic adsorbent, a chemical adsorbent, etc. at a rate of 200 g/L is impregnated into the liner It was a member.
- a glass fiber blended paper (manufactured by Oji Ftex Co., Ltd.) paper having a basis weight of 50 g/m 2 was used as a corrugated base paper and impregnated with an adsorbent dispersion liquid containing activated carbon, an inorganic adsorbent, a chemical adsorbent, etc. at a ratio of 200 g/L.
- the corrugated base material was corrugated to form a corrugated member, and then a liner member and a piece of corrugated cardboard were formed. Two types of single-faced corrugated board, small-sized corrugated cardboard and large-sized corrugated board, having different heights and pitches were prepared.
- a small corrugated member having a pitch of 4.9 mm and a height of 2 mm was used for the small piece corrugated board, and a large corrugated member having a pitch of 5.9 mm and a height of 3 mm was used for the large piece corrugated board.
- Got A plurality of these laminated bodies were stacked to obtain a corrugated honeycomb structure equivalent to that shown in FIG.
- each piece of corrugated cardboard was laminated by aligning the ridge direction of the corrugated member.
- the thickness of the corrugated honeycomb structure (length in the depth direction of cells) was set to 15 mm.
- a gas-permeable sheet was adhered to one surface of the obtained corrugated honeycomb structure, and a chemical-supporting spherical activated carbon ((average particle diameter 2 mm, BET specific surface area 930 m of Osaka Gas Chemical Co., Ltd. was used as a filler from the other surface. 2 /g) of which 23 g was filled in. Then, a breathable sheet was also bonded to the other surface to obtain the air filter of Example 1. A polyester mesh (opening 1 mm) was used as the breathable sheet.
- Example 1 An air filter was obtained in the same manner as in Example 1 except that only the large-sized corrugated board used in Example 1 had a structure in which a plurality of liner members and corrugated members were adhered to each other and laminated. A plurality of large-sized corrugated cardboards were laminated by aligning the ridge direction of the corrugated member.
- FIG. 4 is an enlarged photograph taken from the other surface of the air filter of Example 1 before adhering the breathable sheet to the other surface. As shown in FIG. 4, it was confirmed that the smallest diameter cell was hardly filled with the filler and the filling rate did not exceed 50%. Further, it was confirmed that the filler could be filled in most of the large-diameter cells, and the filling rate was at least 25% or more. Particularly, the filling rate of the large-diameter cell (corresponding to the second large-diameter cell 33 in FIG. 1) having a large diameter of the inscribed circle was high. That is, in Example 1, it was possible to confirm whether or not the filler such as activated carbon could be filled while suppressing the increase of the pressure loss by ensuring the cells which are not filled with the filler and through which the gas easily passes.
- the filler such as activated carbon
- Example 2 The air purifying fan equipped with the air filters obtained in Example 1 and Comparative Example 2 was set, and the air purifying fan was sealed in the test chamber so that the air concentration of formaldehyde was 1 ppm, and the air purifying fan was the same as the target air purifier. Operate at a linear velocity (LV) of 1.0 m/s, measure the formaldehyde air concentration for 60 minutes at 5 minute intervals using a formaldehyde meter htv. From the relationship between elapsed time and formaldehyde air concentration, the initial clean The air supply rate (initial CADR) was measured. The results are shown in Table 2.
- LV linear velocity
- an air purifying fan equipped with an air filter that has been subjected to the above treatment, and seal it in a test room (1 m 3 ) so that the concentration of formaldehyde in the air will be 1 ppm, and use the air purifying fan as the target air purifier.
- Operate at the same linear velocity (LV) of 1.0 m/s measure the formaldehyde air concentration for 60 minutes at 5 minute intervals using a formaldehyde meter htv. From the relationship between elapsed time and formaldehyde air concentration, formaldehyde The clean air supply rate (CADR) after loading 20 mg/sheet was measured.
- LV linear velocity
- the air filter of Example 1 exhibited high adsorption performance not only at the initial stage but also after adsorption of 20 mg.
- the air filter filled with the filler such as activated carbon according to the present invention can improve adsorption efficiency and sustainability while suppressing an increase in pressure loss.
- the air filter of the present invention can be used in an air purifier, an air conditioner, a dehumidifier, etc. for the purpose of removing offensive odor components, harmful components and the like.
Abstract
Description
本願は、2019年1月9日に中国国家知識産権局に出願された、出願番号201910020245.3に基づき優先権を主張し、その内容をここに援用する。 The present invention relates to an air filter used for purposes such as deodorization.
The present application claims priority on the basis of application number 201910020245.3, filed with the China Intellectual Property Office on January 9, 2019, the content of which is incorporated herein by reference.
処理対象となる空気は、セルを通過する間に悪臭成分等がコルゲートハニカム構造体に吸着することにより浄化される。
コルゲートハニカム構造体の材質としては、通常吸着剤を付着または含有させた紙が使用されている。
また、吸着効率や持続性を高めることを目的として、コルゲートハニカム構造体のセルに、活性炭等を充填した脱臭フィルタも提案されている(特許文献1)。 In air purifiers and the like, as an air filter used for the purpose of deodorization and the like, a corrugated honeycomb structure having a large number of cells is known by alternately stacking a plurality of liner members and a plurality of corrugated members. ..
The air to be treated is purified by the malodorous components and the like adsorbing to the corrugated honeycomb structure while passing through the cells.
As a material for the corrugated honeycomb structure, paper to which an adsorbent is attached or contained is usually used.
A deodorizing filter in which cells of a corrugated honeycomb structure are filled with activated carbon or the like has also been proposed for the purpose of improving adsorption efficiency and sustainability (Patent Document 1).
そのため、特許文献1のように、コルゲートハニカム構造体のセルに活性炭等を充填したエアフィルタは、実用化に至っていない。 If activated carbon or the like is made fine, it is possible to fill the cell without making it too large. However, in that case, the cells are clogged with fine activated carbon and the like, resulting in a very high pressure loss.
Therefore, the air filter in which the cells of the corrugated honeycomb structure are filled with activated carbon or the like as in
[1]第1の面と第2の面を有する面状のエアフィルタであって、
面方向に配列する複数のセルを画するコルゲートハニカム構造体と、前記複数のセルに充填された複数の多孔質の充填剤とを備え、
前記複数のセルは、複数の最小径セルと複数の大径セルからなり、
前記複数の最小径セルは、内接円の直径が最も小さいセルであり、
前記複数の大径セルは、内接円の直径が前記複数の最小径セルの内接円の直径よりも大きいセルであり、
前記最小径セルの個数に占める、前記充填剤が充填された最小径セルの個数の割合は50%以下であり、
前記大径セルの個数に占める、前記充填剤が充填された大径セルの個数の割合は25~100%であることを特徴とするエアフィルタ。
[2]前記複数のセルに占める前記最小径セルの割合が10~90面積%である[1]に記載のエアフィルタ。
[3]前記コルゲートハニカム構造体は、複数のライナー部材と複数のコルゲート部材とが互いに接着されて構成されており、
前記複数のライナー部材は、前記面方向に垂直な方向から観察した際に直線状であり、
前記複数のコルゲート部材は、前記面方向に垂直な方向から観察した際に前記ライナー部材が延伸する方向に添って山部と谷部が繰り返す波型形状であり、
前記複数のコルゲート部材は、前記波型形状の高さ及びピッチの一方又は両方が異なる二種以上のコルゲート部材を含む、[1]または[2]に記載のエアフィルタ。
[4]前記複数のコルゲート部材は、前記ライナー部材を介することなく、互いの山部が直接接着されている一対以上のコルゲート部材を含む、[3]に記載のエアフィルタ。
[5]吸着剤が前記コルゲートハニカム構造体に保持されている、[1]~[4]の何れかに記載のエアフィルタ。
[6]前記複数の充填剤が球状である、[1]~[5]の何れかに記載のエアフィルタ。
[7]前記充填剤は活性炭である、[1]~[6]の何れかに記載のエアフィルタ。
[8]前記第1の面及び前記第2の面の一方又は両方に、通気性シートが配置されている、[1]~[7]の何れかに記載のエアフィルタ。 The present invention has the following features to attain the object mentioned above.
[1] A planar air filter having a first surface and a second surface,
A corrugated honeycomb structure that defines a plurality of cells arranged in the surface direction, and a plurality of porous fillers filled in the plurality of cells,
The plurality of cells comprises a plurality of smallest diameter cells and a plurality of large diameter cells,
The plurality of smallest diameter cells are cells having the smallest diameter of the inscribed circle,
The plurality of large-diameter cells is a cell in which the diameter of the inscribed circle is larger than the diameter of the inscribed circle of the plurality of smallest-diameter cells,
The ratio of the number of the minimum diameter cells filled with the filler to the number of the minimum diameter cells is 50% or less,
The air filter, wherein the ratio of the number of the large-sized cells filled with the filler in the number of the large-sized cells is 25 to 100%.
[2] The air filter according to [1], wherein the ratio of the smallest diameter cell to the plurality of cells is 10 to 90 area %.
[3] The corrugated honeycomb structure is configured by bonding a plurality of liner members and a plurality of corrugated members to each other,
The plurality of liner members are linear when observed from a direction perpendicular to the surface direction,
The plurality of corrugated members has a corrugated shape in which peaks and valleys are repeated along the direction in which the liner member extends when observed from a direction perpendicular to the surface direction,
The air filter according to [1] or [2], wherein the plurality of corrugated members include two or more kinds of corrugated members having different heights and/or pitches of the corrugated shape.
[4] The air filter according to [3], wherein the plurality of corrugated members include a pair or more of corrugated members whose peaks are directly bonded to each other without interposing the liner member.
[5] The air filter according to any one of [1] to [4], wherein an adsorbent is held by the corrugated honeycomb structure.
[6] The air filter according to any one of [1] to [5], wherein the plurality of fillers are spherical.
[7] The air filter according to any one of [1] to [6], wherein the filler is activated carbon.
[8] The air filter according to any one of [1] to [7], wherein a breathable sheet is arranged on one or both of the first surface and the second surface.
図1は、本発明の一実施形態に係るエアフィルタに用いるコルゲートハニカム構造体1を面方向に垂直な方向から見た図である。コルゲートハニカム構造体1は、ライナー部材10とコルゲート部材20で構成されており、図1における紙面表側が第1の面61、紙面裏側が第2の面62となる面状体である。
コルゲートハニカム構造体の厚さ(後述する、コルゲートハニカム構造体が有するセルの深さ方向の長さ)は、5~100mmの範囲で調整すればよく、通常、5~50mmである。 The air filter of the present invention comprises a corrugated honeycomb structure defining a plurality of cells arranged in the plane direction, and a plurality of porous fillers filled in the plurality of cells.
FIG. 1 is a view of a
The thickness of the corrugated honeycomb structure (the length in the depth direction of the cells of the corrugated honeycomb structure, which will be described later) may be adjusted in the range of 5 to 100 mm, and usually 5 to 50 mm.
コルゲート部材20は、図1に示すように、細帯状の部材が繰り返し折れ曲がり、面方向に垂直な方向から観察した際にライナー部材10が延伸する方向に添って山部と谷部が繰り返す波型形状とされた部材である。 As shown in FIG. 1, the
As shown in FIG. 1, the
図2に示すように、小コルゲート部材21の谷部21bは1枚のライナー部材10に接着されており、山部21aは、他の1枚のライナー部材10に接着されている。
これに対し、大コルゲート部材22の谷部22bは1枚のライナー部材10に接着されているが、山部22aは、他の1枚のライナー部材10を介することなく、他の大コルゲート部材22の山部22aに直接接着されている。 In this embodiment, two kinds of
As shown in FIG. 2, the
On the other hand, the
本実施形態では、セル30として、最小径セル31と2種類の大径セル(第1大径セル32、第2大径セル33)が形成されている。
最小径セル31は、ライナー部材10と小コルゲート部材21により画された空間である。第1大径セル32は、ライナー部材10と大コルゲート部材22により画された空間である。また、第2大径セル33は、互いの山部22aが直接接着された一対の大コルゲート部材22により画された空間である。 As shown in FIGS. 1 and 2, in the
In the present embodiment, as the
The
これらの内接円の内、最小径内接円41の直径が最も小さく、第1大径内接円42と第2大径内接円43の直径は最小径内接円41の直径よりも大きい。また、第2大径内接円43の直径は第1大径内接円42の直径よりも大きい。 In FIG. 2, a minimum diameter inscribed
Of these inscribed circles, the smallest diameter inscribed
また、本実施形態のように、内接円の直径が異なる複数種類の大径セル(第1大径セル32、第2大径セル33)が存在すると、圧力損失の上昇を抑制する効果がさらに高まると共に、長期間使用した際、同時に目詰まりを生じることを防ぐことができる。また、大きさの異なる複数種類の充填剤を充填しやすい。そのため、吸着特性の異なる複数種類の充填剤を使用しやすい。 In addition, the first large-
In addition, as in the present embodiment, when there are a plurality of types of large-diameter cells (first large-
前記割合が好ましい下限値以上であれば、通気性を確保して、圧力損失の上昇を抑制しやすい。また、前記割合が好ましい上限値以下であれば、第1大径セル32と第2大径セル33に、充分な量の充填剤を充填しやすい。
第1大径セル32の総面積と第2大径セル33の総面積は、充填する充填剤の大きさごとの配合量に応じて適宜調整すればよい。 The ratio of the total area of the
When the ratio is equal to or higher than the preferable lower limit value, it is easy to secure air permeability and suppress an increase in pressure loss. Further, when the ratio is equal to or less than the preferable upper limit value, it is easy to fill the first
The total area of the first large-
最小径内接円41の直径が好ましい範囲の下限値以上であれば、最小径セル31の気体通過を妨げにくい。最小径内接円41の直径が好ましい範囲の上限値以下であれば、最小径セル31を通過する気体を充分にコルゲートハニカム構造体1に接触させて、悪臭成分等をコルゲートハニカム構造体1に吸着させることができる。 The diameter of the smallest diameter inscribed
When the diameter of the smallest diameter inscribed
上記好ましい比率以上であれば、最小径セル31に対する充填剤の充填を抑制しつつ第1大径セル32、第2大径セル33に充填剤を充填しやすい。 The diameters of the first large diameter inscribed
When the ratio is equal to or more than the preferable ratio, it is easy to fill the first
第1大径内接円42の直径が好ましい範囲の下限値以上であれば、第1大径セル32に充填剤を充填しやすい。第1大径内接円42の直径が好ましい範囲の上限値以下であれば、第1大径セル32の面積が過大とならず、コルゲートハニカム構造体1の強度を確保しやすい。 The diameter of the first large diameter inscribed
When the diameter of the first large-diameter inscribed
上記好ましい比率以上であれば、第1大径セル32及び第2大径セル33を利用して、異なる大きさの充填剤を充填しやすい。 The diameter of the second large diameter inscribed
When the ratio is equal to or more than the above preferable ratio, it is easy to fill the fillers of different sizes by using the first
具体的には、小コルゲート部材21の波型形状のピッチは、2~7mmであることが好ましく、3~6mmであることがより好ましい。
また、小コルゲート部材21の波型形状の高さは、0.5~3mmであることが好ましく、1~2.5mmであることがより好ましい。
なお、小コルゲート部材21の波型形状の高さは、小コルゲート部材21の一方の面における谷部21bと山部21aの高さ方向における距離であり、高さ方向とは、ライナー部材10に直交する方向である。 The pitch and height of the corrugated shape of the small
Specifically, the pitch of the corrugated shape of the small
The corrugated height of the small
The corrugated height of the small
具体的には、大コルゲート部材22の波型形状のピッチは、4~12mmであることが好ましく、5~10mmであることがより好ましい。
また、大コルゲート部材22の波型形状の高さは、2~6mmであることが好ましく、2.5~5mmであることがより好ましい。
なお、大コルゲート部材22の波型形状の高さは、大コルゲート部材22の一方の面における谷部22bと山部22aの高さ方向における距離であり、高さ方向とは、ライナー部材10に直交する方向である。 Further, the pitch and height of the corrugated shape of the large
Specifically, the corrugated pitch of the large
The corrugated height of the large
The corrugated height of the large
基材としては、紙類、不織布類、プラスチックフイルム類などシート状の基材であれば、特に限定するものではないが、吸着剤を保持しやすい点から繊維基材が好ましい。繊維基材としては、セルロース繊維を主成分とする紙基材、合成繊維を主成分とするプラスチック基材が挙げられる。中でも、セルロース繊維を主成分とする紙基材が好ましい。
なお、「主成分とする」とは、基材全体に対する割合が50質量%以上であることを意味する。 The
The base material is not particularly limited as long as it is a sheet-shaped base material such as papers, non-woven fabrics and plastic films, but a fiber base material is preferable from the viewpoint of easily holding the adsorbent. Examples of the fiber substrate include a paper substrate containing cellulose fiber as a main component and a plastic substrate containing synthetic fiber as a main component. Of these, a paper base material containing cellulose fibers as a main component is preferable.
In addition, "to be a main component" means that the ratio to the whole base material is 50% by mass or more.
これらのパルプは1種を単独で用いてもよく、2種以上を組み合わせて用いてもよい。 The wood pulp may have been subjected to a cooking process and/or a bleaching process. In general, wood pulp is used after being subjected to various cooking and bleaching steps in order to remove components other than cellulose from the raw material wood. In the present invention, the cooking step and the bleaching step are not particularly limited, and a known method can be appropriately used.
These pulps may be used alone or in combination of two or more.
紙基材は、サイズ剤、紙力増強剤、着色剤、防腐剤、難燃剤等の内添薬品を含んでいてもよい。内添薬品としては、公知のものを用いることができる。 The paper substrate may further contain fibers other than cellulose fibers. Examples of other fibers include rayon fibers, polyethylene fibers, polypropylene fibers, polyester fibers and other synthetic fibers, glass fibers, ceramic fibers, mineral fibers and other inorganic fibers, and animal fibers.
The paper base material may contain internal additives such as a sizing agent, a paper strengthening agent, a coloring agent, a preservative, and a flame retardant. Known internal additives can be used.
基材の坪量は、10~500g/m2であることが好ましく、10~400g/m2であることがより好ましく、10~300g/m2であることがさらに好ましい。
繊維基材は、抄紙法により得たものが好ましい。 Examples of the plastic substrate include those containing, as a main component, one or more kinds of synthetic fibers such as rayon fiber, polyethylene fiber, polypropylene fiber and polyester fiber.
The basis weight of the base material is preferably 10 to 500 g/m 2 , more preferably 10 to 400 g/m 2 , and even more preferably 10 to 300 g/m 2 .
The fiber base material is preferably obtained by a papermaking method.
基材に保持させる吸着剤は、基材内部に保持されていても、表面に付着していても、内部及び表面の双方に存在していてもよい。
基材に保持させる吸着剤は、抄紙時に内添してもよいし、抄紙後に塗布または含浸させてもよい。 Examples of the adsorbent to be held on the base material include known adsorbents such as granular, powdery, fibrous and the like activated carbon, mordenite, ferrierite, molecular sieves and other zeolites, silica gel and alumina gel. A chemical that reacts with the component to be removed (for example, a compound that reacts with ammonia or formaldehyde) may be carried on these adsorbents. Alternatively, a chemical that reacts with the component to be removed may be directly supported on the base material.
The adsorbent to be held on the base material may be held inside the base material, adhered to the surface, or present both inside and on the surface.
The adsorbent to be held on the substrate may be added internally during paper making, or may be applied or impregnated after paper making.
すなわち、小片段ボールとX構造フルートとを積層接着してコルゲートハニカム構造体1を製造すると、1つの片段ボールを構成するライナー部材10が単独で存在する部分と、一対の片段ボールを構成する2枚のライナー部材10とが重なった状態で存在する部分とが形成される。 When laminating and bonding the
That is, when the
充填剤50は粒状であることが好ましく、略球状であることがより好ましく、球状であることが特に好ましい。球状または略球状であれば、セル30への充填が容易であると共に、セル30を画するライナー部材10やコルゲート部材20との間に適度な隙間が生じ、通気を確保しやすい。 The
The
充填剤50の比表面積が前記好ましい下限値以上であることにより、悪臭成分等の吸着性能を発揮しやすい。また、充填剤50の比表面積が前記好ましい上限値以下であることにより、充填剤50の強度を保ちやすい。 The specific surface area of the
When the specific surface area of the
最小径セル31の充填率が好ましい上限値以下であれば、通気性を確保しやすい。
最小径セル31の充填率を好ましい上限値以下とするためには、最小径内接円41よりも直径の小さい充填剤50が充填剤50全体に占める割合を低くすればよい。
最小径セル31の充填率の下限は0%であってもよい。すなわち、最小径セル31には、充填剤50が充填されていなくてもよい。 The ratio (filling rate) of the number of the
If the filling rate of the
In order to set the filling rate of the
The lower limit of the filling rate of the
大径セルの充填率が好ましい下限値以上であれば、充填剤50によって吸着効率や持続性を高めやすい。大径セルの充填率が好ましい上限値以下であれば充填作業が容易である。
なお、充填率を求めるにあたっては、充填剤50の大きさにかかわらず、1個でも充填されているセルは充填されたセルとする。 On the other hand, the ratio of the number of large-diameter cells filled with the
When the filling rate of the large-diameter cell is equal to or higher than the preferable lower limit value, it is easy to increase the adsorption efficiency and sustainability by the
In determining the filling rate, cells filled with at least one filling agent are treated as filled cells regardless of the size of the filling
小充填剤51の直径は、最小径内接円41より大きいことが好ましい。これにより、小充填剤51が最小径セル31に充填されにくくなる。
なお、充填剤50の直径が最小径内接円41より大きくても、割れるなどにより、最小径セル31に破片となった充填剤50などが充填される場合がある。 FIG. 3 schematically shows an example in which a spherical
The diameter of the
Even if the diameter of the
通気性シート71、通気性シート72は、コルゲートハニカム構造体1の第1の面61値と第2の面62に各々接着して配置されている。
通気性シート71と通気性シート72を位置することにより、エアフィルタから充填剤50が脱落することを防止できる。また、エアフィルタを通る気体から、塵などを除去することができる。 The
The
By positioning the
また、大径セルは、図1、2に示したように2種類に限られず、1種類であっても、3種類以上であってもよい。
また、セル30の形状にも特に限定はない。
また、図1、2では、大コルゲート部材22と小コルゲート部材21が、ピッチと高さの双方で異なる構成としたが、ピッチと高さの一方のみ異なる複数種類のコルゲート部材20を使用してもよい。
また、セル30が異なる大きさのセルを含むことができれば、コルゲート部材20は一種類でもよい。例えば、一種類の片段ボールを用いて作成したX構造フルートを複数積層してもよい。
また、充填剤50の形や大きさは図3に示したように2種類に限られず、3種類以上でもよい。 Although the
The large-diameter cell is not limited to two types as shown in FIGS. 1 and 2, and may be one type or three or more types.
Also, the shape of the
Further, in FIGS. 1 and 2, the large
Further, the
The shape and size of the
坪量50g/m2のガラス繊維混抄紙(王子エフテックス社製)をライナー原紙とし、活性炭、無機吸着剤、化学吸着剤等を200g/Lの割合で含む吸着剤分散液を含浸させてライナー部材とした。
坪量50g/m2のガラス繊維混抄紙(王子エフテックス社製)紙をコルゲート原紙とし、活性炭、無機吸着剤、化学吸着剤等を200g/Lの割合で含む吸着剤分散液を含浸させてコルゲート用基材とした。
コルゲート用基材をコルゲート処理してコルゲート部材とした後、ライナー部材と貼り合せ片段ボールを形成した。片段ボールは、高さ及びピッチの異なる、小片段ボールと大片段ボールの2種類を作成した。小片段ボールには、ピッチが4.9mm、高さが2mmの小コルゲート部材を用い、大片段ボールには、ピッチが5.9mm、高さが3mmの大コルゲート部材を用いた。 [Example 1]
A glass fiber mixed paper (manufactured by Oji Ftex Co., Ltd.) having a basis weight of 50 g/m 2 is used as a liner base paper, and an adsorbent dispersion liquid containing activated carbon, an inorganic adsorbent, a chemical adsorbent, etc. at a rate of 200 g/L is impregnated into the liner It was a member.
A glass fiber blended paper (manufactured by Oji Ftex Co., Ltd.) paper having a basis weight of 50 g/m 2 was used as a corrugated base paper and impregnated with an adsorbent dispersion liquid containing activated carbon, an inorganic adsorbent, a chemical adsorbent, etc. at a ratio of 200 g/L. Used as a corrugated substrate.
The corrugated base material was corrugated to form a corrugated member, and then a liner member and a piece of corrugated cardboard were formed. Two types of single-faced corrugated board, small-sized corrugated cardboard and large-sized corrugated board, having different heights and pitches were prepared. A small corrugated member having a pitch of 4.9 mm and a height of 2 mm was used for the small piece corrugated board, and a large corrugated member having a pitch of 5.9 mm and a height of 3 mm was used for the large piece corrugated board.
通気性シートとしては、ポリエステル製のメッシュ(目開き1mm)を用いた。 A gas-permeable sheet was adhered to one surface of the obtained corrugated honeycomb structure, and a chemical-supporting spherical activated carbon ((average particle diameter 2 mm, BET specific surface area 930 m of Osaka Gas Chemical Co., Ltd. was used as a filler from the other surface. 2 /g) of which 23 g was filled in. Then, a breathable sheet was also bonded to the other surface to obtain the air filter of Example 1.
A polyester mesh (opening 1 mm) was used as the breathable sheet.
実施例1で用いた大片段ボールのみを、互いのライナー部材とコルゲート部材とを接着して複数積層した構造にした以外は実施例1と同様にしてエアフィルタを得た。なお、複数の大片段ボールはコルゲート部材の稜線方向を揃えて積層した。 [Comparative Example 1]
An air filter was obtained in the same manner as in Example 1 except that only the large-sized corrugated board used in Example 1 had a structure in which a plurality of liner members and corrugated members were adhered to each other and laminated. A plurality of large-sized corrugated cardboards were laminated by aligning the ridge direction of the corrugated member.
得られたエアフィルタを100mm×100mmの開口の樹脂ケースに入れた後、風洞装置にセットし、0.5m/s、1.0m/s、1.5m/s、2.0m/sの各線速時の圧力損出を測定した。
結果を表1に示す。 [Pressure loss evaluation]
After putting the obtained air filter in a resin case with an opening of 100 mm × 100 mm, set it in a wind tunnel device, and each line of 0.5 m/s, 1.0 m/s, 1.5 m/s, 2.0 m/s The pressure loss at high speed was measured.
The results are shown in Table 1.
図4は、実施例1のエアフィルタの他方の面に通気性シートを接着する前に、他方の面側から撮影した拡大写真である。図4に示すように、最小径セルには、ほとんど充填剤が充填されず、充填率が50%を超えないことが確認できた。また、大径セルの大部分に充填剤を充填することができ、少なくとも25%以上の充填率となったことが確認できた。特に、内接円の直径が大きい大径セル(図1の第2大径セル33に相当)の充填率が高かった。
すなわち、実施例1では、充填剤が充填されておらず気体が通過しやすいセルを確保して圧力損失の上昇を抑制しながら、活性炭等の充填剤を充填できたことか確認できた。 As shown in Table 1, it can be seen that the air filter of Example 1 is superior to Comparative Example 1 in terms of pressure loss.
FIG. 4 is an enlarged photograph taken from the other surface of the air filter of Example 1 before adhering the breathable sheet to the other surface. As shown in FIG. 4, it was confirmed that the smallest diameter cell was hardly filled with the filler and the filling rate did not exceed 50%. Further, it was confirmed that the filler could be filled in most of the large-diameter cells, and the filling rate was at least 25% or more. Particularly, the filling rate of the large-diameter cell (corresponding to the second large-
That is, in Example 1, it was possible to confirm whether or not the filler such as activated carbon could be filled while suppressing the increase of the pressure loss by ensuring the cells which are not filled with the filler and through which the gas easily passes.
実施例1において、球状活性炭を充填しなかった以外は実施例1と同様にエアフィルタを得た。 [Comparative Example 2]
An air filter was obtained in the same manner as in Example 1 except that spherical activated carbon was not filled.
中国GB規格(GB/T 18801-2015)に基づく評価試験を採用し、試験室の大きさを1m3とした簡易試験により、エアフィルタのホルムアルデヒド負荷後のクリーンエア供給率(CADR)及びクリーンエア供給率維持率(CADR維持率)を測定することにより、ホルムアルデヒド除去性能評価を行った。 [Formaldehyde removal performance evaluation]
Adopted an evaluation test based on the Chinese GB standard (GB/T 18801-2015) and conducted a simple test with a test chamber size of 1 m 3 to show the clean air supply rate (CADR) and clean air after formaldehyde loading of the air filter. The formaldehyde removal performance was evaluated by measuring the supply rate maintenance rate (CADR maintenance rate).
実施例1、比較例2で得られたエアフィルタを搭載した空清ファンをセットし、ホルムアルデヒドの気中濃度を1ppmとなるように試験室に封入し、空清ファンを対象となる空気清浄機と同じ線速(LV)である1.0m/sで稼働させ、ホルムアルデヒドメーターhtvを用いて、5分間隔でホルムアルデヒド気中濃度を60分間測定し、経過時間とホルムアルデヒド気中濃度の関係から、初期クリーンエア供給率(初期CADR)を測定した。
結果を表2に示す。 (Measurement of initial CADR)
The air purifying fan equipped with the air filters obtained in Example 1 and Comparative Example 2 was set, and the air purifying fan was sealed in the test chamber so that the air concentration of formaldehyde was 1 ppm, and the air purifying fan was the same as the target air purifier. Operate at a linear velocity (LV) of 1.0 m/s, measure the formaldehyde air concentration for 60 minutes at 5 minute intervals using a formaldehyde meter htv. From the relationship between elapsed time and formaldehyde air concentration, the initial clean The air supply rate (initial CADR) was measured.
The results are shown in Table 2.
次に、実施例1、比較例2で得られたエアフィルタを搭載した空清ファンをセットし、揮散用ファン上の濾紙にホルムアルデヒド溶液を、ホルムアルデヒドの質量が20mgとなるように含浸させ、空清ファン及び揮散ファンを稼働させ、12時間放置した。 (Measurement of CADR after loading with formaldehyde)
Next, an air purifying fan equipped with the air filters obtained in Example 1 and Comparative Example 2 was set, and the filter paper on the volatilization fan was impregnated with the formaldehyde solution so that the mass of formaldehyde was 20 mg. And the volatilization fan was operated and left for 12 hours.
本発明のエアフィルタは、悪臭成分や有害成分等の除去を目的として、空気清浄機、エアコン、除湿機等に使用することができる。 The air filter filled with the filler such as activated carbon according to the present invention can improve adsorption efficiency and sustainability while suppressing an increase in pressure loss.
The air filter of the present invention can be used in an air purifier, an air conditioner, a dehumidifier, etc. for the purpose of removing offensive odor components, harmful components and the like.
10 ライナー部材
20 コルゲート部材
21 小コルゲート部材
22 大コルゲート部材
30 セル
31 最小径セル
32 第1大径セル
33 第2大径セル
41 最小径内接円
42 第1大径内接円
43 第2大径内接円
50 充填剤
51 小充填剤
52 大充填剤
61 第1の面
62 第2の面
71 通気性シート
72 通気性シート 1
Claims (8)
- 第1の面と第2の面を有する面状のエアフィルタであって、
面方向に配列する複数のセルを画するコルゲートハニカム構造体と、前記複数のセルに充填された複数の多孔質の充填剤とを備え、
前記複数のセルは、複数の最小径セルと複数の大径セルからなり、
前記複数の最小径セルは、内接円の直径が最も小さいセルであり、
前記複数の大径セルは、内接円の直径が前記複数の最小径セルの内接円の直径よりも大きいセルであり、
前記最小径セルの個数に占める、前記充填剤が充填された最小径セルの個数の割合は50%以下であり、
前記大径セルの個数に占める、前記充填剤が充填された大径セルの個数の割合は25~100%であることを特徴とするエアフィルタ。 A planar air filter having a first surface and a second surface,
A corrugated honeycomb structure that defines a plurality of cells arranged in the surface direction, and a plurality of porous fillers filled in the plurality of cells,
The plurality of cells comprises a plurality of smallest diameter cells and a plurality of large diameter cells,
The plurality of smallest diameter cells are cells having the smallest diameter of the inscribed circle,
The plurality of large-diameter cells is a cell in which the diameter of the inscribed circle is larger than the diameter of the inscribed circle of the plurality of smallest-diameter cells,
The ratio of the number of the minimum diameter cells filled with the filler to the number of the minimum diameter cells is 50% or less,
The air filter, wherein the ratio of the number of the large-sized cells filled with the filler in the number of the large-sized cells is 25 to 100%. - 前記複数のセルに占める前記最小径セルの割合が10~90面積%である、請求項1に記載のエアフィルタ。 The air filter according to claim 1, wherein the ratio of the smallest diameter cell to the plurality of cells is 10 to 90 area %.
- 前記コルゲートハニカム構造体は、複数のライナー部材と複数のコルゲート部材とが互いに接着されて構成されており、
前記複数のライナー部材は、前記面方向に垂直な方向から観察した際に直線状であり、
前記複数のコルゲート部材は、前記面方向に垂直な方向から観察した際に前記ライナー部材が延伸する方向に添って山部と谷部が繰り返す波型形状であり、
前記複数のコルゲート部材は、前記波型形状の高さ及びピッチの一方又は両方が異なる二種以上のコルゲート部材を含む、請求項1または2に記載のエアフィルタ。 The corrugated honeycomb structure is configured by bonding a plurality of liner members and a plurality of corrugated members to each other,
The plurality of liner members are linear when observed from a direction perpendicular to the surface direction,
The plurality of corrugated members has a corrugated shape in which peaks and valleys are repeated along the direction in which the liner member extends when observed from a direction perpendicular to the surface direction,
The air filter according to claim 1 or 2, wherein the plurality of corrugated members include two or more types of corrugated members having different heights and/or pitches of the corrugated shape. - 前記複数のコルゲート部材は、前記ライナー部材を介することなく、互いの山部が直接接着されている一対以上のコルゲート部材を含む、請求項3に記載のエアフィルタ。 The air filter according to claim 3, wherein the plurality of corrugated members include a pair of corrugated members whose peaks are directly bonded to each other without the liner member interposed therebetween.
- 吸着剤が前記コルゲートハニカム構造体に保持されている、請求項1~4の何れか一項に記載のエアフィルタ。 The air filter according to any one of claims 1 to 4, wherein an adsorbent is held by the corrugated honeycomb structure.
- 前記複数の充填剤が球状である、請求項1~5の何れか一項に記載のエアフィルタ。 The air filter according to any one of claims 1 to 5, wherein the plurality of fillers are spherical.
- 前記充填剤は活性炭である、請求項1~6の何れか一項に記載のエアフィルタ。 The air filter according to any one of claims 1 to 6, wherein the filler is activated carbon.
- 前記第1の面及び前記第2の面の一方又は両方に、通気性シートが配置されている、請求項1~7の何れか一項に記載のエアフィルタ。 The air filter according to any one of claims 1 to 7, wherein a breathable sheet is arranged on one or both of the first surface and the second surface.
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