JPWO2020145345A1 - Air filter - Google Patents

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JPWO2020145345A1
JPWO2020145345A1 JP2020565202A JP2020565202A JPWO2020145345A1 JP WO2020145345 A1 JPWO2020145345 A1 JP WO2020145345A1 JP 2020565202 A JP2020565202 A JP 2020565202A JP 2020565202 A JP2020565202 A JP 2020565202A JP WO2020145345 A1 JPWO2020145345 A1 JP WO2020145345A1
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diameter
cells
corrugated
air filter
filler
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健太郎 田中
卓 尾林
健太郎 甲斐
正千代 今西
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New Oji Paper Co Ltd
Osaka Gas Chemicals Co Ltd
Oji Holdings Corp
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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D53/00Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/02Separation 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
    • B01D53/04Separation 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
    • B01D53/0407Constructional details of adsorbing systems
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    • 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
    • A61L9/01Deodorant compositions
    • 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
    • A61L9/01Deodorant compositions
    • A61L9/014Deodorant compositions containing sorbent material, e.g. activated carbon
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D46/00Filters or filtering processes specially modified for separating dispersed particles from gases or vapours
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D46/00Filters or filtering processes specially modified for separating dispersed particles from gases or vapours
    • B01D46/0027Filters or filtering processes specially modified for separating dispersed particles from gases or vapours with additional separating or treating functions
    • B01D46/0036Filters or filtering processes specially modified for separating dispersed particles from gases or vapours with additional separating or treating functions by adsorption or absorption
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D46/00Filters or filtering processes specially modified for separating dispersed particles from gases or vapours
    • B01D46/24Particle separators, e.g. dust precipitators, using rigid hollow filter bodies
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D46/00Filters or filtering processes specially modified for separating dispersed particles from gases or vapours
    • B01D46/24Particle separators, e.g. dust precipitators, using rigid hollow filter bodies
    • B01D46/2403Particle separators, e.g. dust precipitators, using rigid hollow filter bodies characterised by the physical shape or structure of the filtering element
    • B01D46/2418Honeycomb filters
    • B01D46/2425Honeycomb filters characterized by parameters related to the physical properties of the honeycomb structure material
    • B01D46/2429Honeycomb filters characterized by parameters related to the physical properties of the honeycomb structure material of the honeycomb walls or cells
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D46/00Filters or filtering processes specially modified for separating dispersed particles from gases or vapours
    • B01D46/24Particle separators, e.g. dust precipitators, using rigid hollow filter bodies
    • B01D46/2403Particle separators, e.g. dust precipitators, using rigid hollow filter bodies characterised by the physical shape or structure of the filtering element
    • B01D46/2418Honeycomb filters
    • B01D46/2451Honeycomb filters characterized by the geometrical structure, shape, pattern or configuration or parameters related to the geometry of the structure
    • B01D46/248Structures comprising laminated bodies or discs
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D46/00Filters or filtering processes specially modified for separating dispersed particles from gases or vapours
    • B01D46/24Particle separators, e.g. dust precipitators, using rigid hollow filter bodies
    • B01D46/2403Particle separators, e.g. dust precipitators, using rigid hollow filter bodies characterised by the physical shape or structure of the filtering element
    • B01D46/2418Honeycomb filters
    • B01D46/2451Honeycomb filters characterized by the geometrical structure, shape, pattern or configuration or parameters related to the geometry of the structure
    • B01D46/2482Thickness, height, width, length or diameter
    • 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
    • B01D53/02Separation 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
    • B01D53/04Separation 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
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J20/00Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
    • B01J20/02Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material
    • B01J20/20Solid 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
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D2253/00Adsorbents used in seperation treatment of gases and vapours
    • B01D2253/10Inorganic adsorbents
    • B01D2253/102Carbon

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Abstract

圧力損失の上昇を抑制しながら、吸着効率や持続性を高めた、活性担当の充填剤を充填したエアフィルタを提供する。本発明のエアフィルタは、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(30)を画するコルゲートハニカム構造体(1)と、前記複数のセル(30)に充填された複数の多孔質の充填剤(50)とを備え、前記複数のセル(30)は、複数の最小径セル(31)と複数の大径セル(第1大径セル(32)、第2大径セル(33))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(31)の個数に占める、前記充填剤が充填された最小径セル(31)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。Provided is an air filter filled with a filler in charge of activation, which has improved adsorption efficiency and sustainability while suppressing an increase in pressure loss. The air filter of the present invention is a planar air filter having a first surface and a second surface, and has a corrugated honeycomb structure (1) defining a plurality of cells (30) arranged in the surface direction. The plurality of cells (30) include a plurality of porous fillers (50) filled in the plurality of cells (30), and the plurality of cells (30) include a plurality of minimum diameter cells (31) and a plurality of large diameter cells (first). It is composed of one large diameter cell (32) and a second large diameter cell (33), and the plurality of minimum diameter cells are cells having the smallest diameter of the inscribed circle, and the plurality of large diameter cells are inscribed. The number of minimum diameter cells (31) filled with the filler, which is a cell in which the diameter of the circle is larger than the diameter of the inscribed circle of the plurality of minimum diameter cells and occupies the number of the minimum diameter cells (31). The ratio of the number of large-diameter cells to the number of the large-diameter cells is 25 to 100%, and the ratio of the number of large-diameter cells filled with the filler is 25 to 100%.

Description

本発明は、脱臭等の目的で使用するエアフィルタに関する。
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 a purpose such as deodorization.
This application claims priority based on application number 201910020245.3., Which was filed with the China National Intellectual Property Office on January 9, 2019, and the contents thereof are incorporated herein by reference.

空気清浄機等において、脱臭等の目的で使用されるエアフィルタとしては、複数のライナー部材と複数のコルゲート部材とを交互に重ねることにより多数のセルを構成したコルゲートハニカム構造体が知られている。
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)。
As an air filter used for the purpose of deodorizing in an air purifier or the like, a corrugated honeycomb structure in which a large number of cells are formed by alternately stacking a plurality of liner members and a plurality of corrugated members is known. ..
The air to be treated is purified by adsorbing malodorous components and the like on the corrugated honeycomb structure while passing through the cell.
As the material of the corrugated honeycomb structure, paper to which an adsorbent is attached or contained is usually used.
Further, for the purpose of improving adsorption efficiency and sustainability, a deodorizing filter in which a cell of a corrugated honeycomb structure is filled with activated carbon or the like has also been proposed (Patent Document 1).

特開2003−47649号公報Japanese Unexamined Patent Publication No. 2003-47649

しかし、特許文献1のように、セルに活性炭等を充填するためには、ある程度大きなセルが必要となる。その場合、処理対象となる空気は、セルを通過する間にコルゲートハニカム構造体に充分に接触することができず、コルゲートハニカム構造体の利点である即効性のある吸着性能を発揮しにくくなる。 However, as in Patent Document 1, in order to fill the cell with activated carbon or the like, a cell having a certain size is required. In that case, the air to be treated cannot sufficiently contact the corrugated honeycomb structure while passing through the cell, and it becomes difficult to exhibit the immediate adsorption performance which is an advantage of the corrugated honeycomb structure.

活性炭等を細かくすれば、セルをあまり大きくすることなく充填することが可能である。しかし、その場合、細かい活性炭等によりセルが目詰まりした状態となり、圧力損失が非常に高くなってしまう。
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 finer, it is possible to fill the cell without making it too large. However, in that case, the cell becomes clogged with fine activated carbon or the like, and the pressure loss becomes very high.
Therefore, the air filter in which the cells of the corrugated honeycomb structure are filled with activated carbon or the like as in Patent Document 1 has not been put into practical use.

本発明は、上記事情に鑑みてなされたものであって、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することにより、吸着効率や持続性を高めたエアフィルタを提供することを課題とする。 The present invention has been made in view of the above circumstances, and provides an air filter having improved adsorption efficiency and sustainability by filling with a filler such as activated carbon while suppressing an increase in pressure loss. Is the subject.

上記の課題を達成するために、本発明は以下の構成を採用した。
[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。
In order to achieve the above problems, the present invention has adopted the following configuration.
[1] A planar air filter having a first surface and a second surface.
A corrugated honeycomb structure demarcating a plurality of cells arranged in a plane direction and a plurality of porous fillers filled in the plurality of cells are provided.
The plurality of cells consist of a plurality of minimum diameter cells and a plurality of large diameter cells.
The plurality of minimum diameter cells are the cells having the smallest diameter of the inscribed circle.
The plurality of large-diameter cells are cells in which the diameter of the inscribed circle is larger than the diameter of the inscribed circle of the plurality of minimum-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.
An air filter characterized in that the ratio of the number of large-diameter cells filled with the filler to the number of large-diameter cells is 25 to 100%.
[2] The air filter according to [1], wherein the ratio of the minimum diameter cell to the plurality of cells is 10 to 90 area%.
[3] The corrugated honeycomb structure is configured such that a plurality of liner members and a plurality of corrugated members are bonded to each other.
The plurality of liner members are linear when observed from a direction perpendicular to the plane direction.
The plurality of corrugated members have a wavy shape in which peaks and valleys repeat along the direction in which the liner member extends when observed from a direction perpendicular to the plane direction.
The air filter according to [1] or [2], wherein the plurality of corrugated members include two or more types of corrugated members having different heights and 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 in which mountain portions are directly adhered to each other without interposing the liner member.
[5] The air filter according to any one of [1] to [4], wherein the adsorbent is held in 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.

本発明の活性炭等の充填剤を充填したエアフィルタによれば、圧力損失の上昇を抑制しながら、吸着効率や持続性を高めることができる。 According to the air filter filled with a filler such as activated carbon of the present invention, it is possible to improve the adsorption efficiency and sustainability while suppressing the increase in pressure loss.

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の平面図である。It is a top view of the corrugated honeycomb structure used for the air filter which concerns on one Embodiment of this invention. 図1のコルゲートハニカム構造体の部分拡大図である。It is a partially enlarged view of the corrugated honeycomb structure of FIG. 本発明の一実施形態に係るエアフィルタの断面図である。It is sectional drawing of the air filter which concerns on one Embodiment of this invention. 実施例に係るエアフィルタの拡大写真である。It is an enlarged photograph of the air filter which concerns on Example.

本発明のエアフィルタは、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る。
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 includes a corrugated honeycomb structure that demarcates 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 the corrugated honeycomb structure 1 used in the air filter according to the embodiment of the present invention as viewed from a direction perpendicular to the 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 the first surface 61 and the back side of the paper surface is the second surface 62.
The thickness of the corrugated honeycomb structure (the length of the corrugated honeycomb structure in the depth direction, which will be described later) may be adjusted in the range of 5 to 100 mm, and is usually 5 to 50 mm.

ライナー部材10は、図1に示すように、面方向に垂直な方向から観察した際に直線状ないし略直線状に見え、図1の紙面厚さ方向に幅のある細帯状の部材である。
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 liner member 10 is a strip-shaped member which looks linear or substantially linear when observed from a direction perpendicular to the plane direction and has a width in the paper surface thickness direction of FIG.
As shown in FIG. 1, the corrugated member 20 has a corrugated shape in which strip-shaped members are repeatedly bent and peaks and valleys are repeated along the direction in which the liner member 10 is stretched when observed from a direction perpendicular to the plane direction. It is a shaped member.

本実施形態では、小コルゲート部材21と大コルゲート部材22の2種類のコルゲート部材20が使用されている。大コルゲート部材22のピッチと高さは、小コルゲート部材21のピッチと高さよりも大きい。
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 types of corrugated members 20 are used, a small corrugated member 21 and a large corrugated member 22. The pitch and height of the large corrugated member 22 is larger than the pitch and height of the small corrugated member 21.
As shown in FIG. 2, the valley portion 21b of the small corrugated member 21 is adhered to one liner member 10, and the mountain portion 21a is adhered to the other liner member 10.
On the other hand, the valley portion 22b of the large corrugated member 22 is adhered to one liner member 10, but the mountain portion 22a is attached to the other large corrugated member 22 without going through the other one liner member 10. It is directly adhered to the mountain portion 22a of.

図1、図2に示すように、コルゲートハニカム構造体1には、ライナー部材10及びコルゲート部材20で画された複数のセル30が面方向に配列するように形成されている。
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, the corrugated honeycomb structure 1 is formed so that a plurality of cells 30 defined by the liner member 10 and the corrugated member 20 are arranged in the plane direction.
In the present embodiment, 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 minimum 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. Further, the second large-diameter cell 33 is a space defined by a pair of large corrugated members 22 to which the mountain portions 22a are directly adhered to each other.

図2において、最小径内接円41は最小径セル31の内接円であり、第1大径内接円42は第1大径セル32の内接円であり、第2大径内接円43は第2大径セル33の内接円である。
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, the minimum diameter inscribed circle 41 is the inscribed circle of the minimum diameter cell 31, the first large diameter inscribed circle 42 is the inscribed circle of the first large diameter cell 32, and the second large diameter inscribed circle 42. The circle 43 is the inscribed circle of the second large-diameter cell 33.
Of these inscribed circles, the diameter of the smallest diameter inscribed circle 41 is the smallest, and the diameters of the first large diameter inscribed circle 42 and the second large diameter inscribed circle 43 are larger than the diameter of the smallest diameter inscribed circle 41. big. Further, the diameter of the second large diameter inscribed circle 43 is larger than the diameter of the first large diameter inscribed circle 42.

最小径内接円41が内接する最小径セル31は、開口面積が小さいため、充填剤が充填されにくく、気体をスムーズに通過させることができる。また、最小径セル31は、開口面積が小さいため、最小径セル31を通過する気体は、ライナー部材10と小コルゲート部材21に充分接触することができ、悪臭成分等をこれらの部材に吸着させやすい。 Since the minimum diameter cell 31 inscribed by the minimum diameter inscribed circle 41 has a small opening area, it is difficult for the filler to be filled and the gas can pass smoothly. Further, since the minimum diameter cell 31 has a small opening area, the gas passing through the minimum diameter cell 31 can sufficiently contact the liner member 10 and the small corrugated member 21, and the malodorous component or the like is adsorbed on these members. Cheap.

また、最小径内接円41よりも直径の大きい内接円が内接する第1大径セル32と第2大径セル33には、最小径セル31には入りにくい充分な大きさの充填剤を充填することができる。そのため、圧力損失の上昇を抑制しながら、充填剤によって吸着効率や持続性を高めることができる。
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。
Further, the first large-diameter cell 32 and the second large-diameter cell 33, in which the inscribed circle having a diameter larger than the minimum-diameter inscribed circle 41 is inscribed, have a sufficient size of filler that is difficult to enter into the minimum-diameter cell 31. Can be filled. Therefore, the adsorption efficiency and sustainability can be improved by the filler while suppressing the increase in pressure loss.
Further, when there are a plurality of types of large-diameter cells (first large-diameter cell 32, second large-diameter cell 33) having different diameters of the inscribed circles as in the present embodiment, the effect of suppressing an increase in pressure loss is obtained. In addition to further increasing, it is possible to prevent clogging at the same time when used for a long period of time. In addition, it is easy to fill a plurality of types of fillers having different sizes. Therefore, it is easy to use a plurality of types of fillers having different adsorption characteristics.

コルゲートハニカム構造体1におけるセル30の総面積(100%)に対する最小径セル31の総面積の割合(コルゲートハニカム構造体1の複数セル30に占める、最小径セル31の割合(面積%)を意味する。)は、10〜90%であることが好ましく、15〜75%であることがより好ましく、20〜50%であることがさらに好ましい。
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 minimum diameter cell 31 to the total area (100%) of the cells 30 in the corrugated honeycomb structure 1 (meaning the ratio (area%) of the minimum diameter cell 31 to the plurality of cells 30 of the corrugated honeycomb structure 1). ) Is preferably 10 to 90%, more preferably 15 to 75%, and even more preferably 20 to 50%.
When the ratio is at least a preferable lower limit value, it is easy to secure air permeability and suppress an increase in pressure loss. Further, when the ratio is not more 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 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.

最小径セル31、第1大径セル32、第2大径セル33は、ライナー部材10が配列する方向において、できるだけ均等に分布していることが好ましい。これにより、部分的に圧力損失が高くなることを防止できる。 It is preferable that the minimum diameter cell 31, the first large diameter cell 32, and the second large diameter cell 33 are distributed as evenly as possible in the direction in which the liner members 10 are arranged. As a result, it is possible to prevent the pressure loss from being partially increased.

最小径内接円41の直径は、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く、1.5〜2.0mmであることがさらに好ましい。
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 minimum diameter inscribed circle 41 is preferably 0.5 to 3 mm, more preferably 1 to 2.5 mm, and even more preferably 1.5 to 2.0 mm.
When the diameter of the minimum diameter inscribed circle 41 is equal to or greater than the lower limit of the preferable range, it is difficult to prevent the gas passage of the minimum diameter cell 31. If the diameter of the minimum diameter inscribed circle 41 is equal to or less than the upper limit of the preferable range, the gas passing through the minimum diameter cell 31 is sufficiently brought into contact with the corrugated honeycomb structure 1, and the malodorous component or the like is transferred to the corrugated honeycomb structure 1. It can be adsorbed.

第1大径内接円42及び第2大径内接円43の直径は、最小径内接円41の直径の1.1倍以上であることが好ましく、1.5倍以上であることがより好ましい。
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 diameter of the first large diameter inscribed circle 42 and the second large diameter inscribed circle 43 is preferably 1.1 times or more, preferably 1.5 times or more the diameter of the minimum diameter inscribed circle 41. More preferred.
When the ratio is more than the above 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 filler in the minimum-diameter cell 31.

第1大径内接円42の直径は、1〜6mmであることが好ましく、1〜4mmであることがより好ましく、2〜3mmであることがさらに好ましい。
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 circle 42 is preferably 1 to 6 mm, more preferably 1 to 4 mm, and even more preferably 2 to 3 mm.
When the diameter of the first large diameter inscribed circle 42 is equal to or greater than the lower limit of the preferable range, the first large diameter cell 32 can be easily filled with the filler. When the diameter of the first large-diameter inscribed circle 42 is not more than the upper limit of the preferable range, the area of the first large-diameter cell 32 does not become excessive, and it is easy to secure the strength of the corrugated honeycomb structure 1.

第2大径内接円43の直径は、第1大径内接円42の直径の1.1倍以上であることが好ましく、1.25倍以上であることがより好ましい。
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 circle 43 is preferably 1.1 times or more, more preferably 1.25 times or more the diameter of the first large-diameter inscribed circle 42.
When the ratio is 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.

小コルゲート部材21の波型形状のピッチ、及び高さは、最小径内接円41の直径が前記好ましい値となるように決めることができる。
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 corrugated member 21 can be determined so that the diameter of the minimum diameter inscribed circle 41 becomes the preferable value.
Specifically, 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 height of the corrugated shape of the small corrugated member 21 is preferably 0.5 to 3 mm, more preferably 1 to 2.5 mm.
The height of the corrugated shape of the small corrugated member 21 is the distance between the valley portion 21b and the mountain portion 21a on one surface of the small corrugated member 21 in the height direction, and the height direction is defined as the liner member 10. The directions are orthogonal.

また、大コルゲート部材22の波型形状のピッチ、及び高さは、第1大径内接円42と第2大径内接円43の直径が前記好ましい値となるように決めることができる。
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 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 preferable values.
Specifically, the wavy pitch of the large corrugated member 22 is preferably 4 to 12 mm, more preferably 5 to 10 mm.
The height of the corrugated shape of the large corrugated member 22 is preferably 2 to 6 mm, more preferably 2.5 to 5 mm.
The height of the corrugated shape of the large corrugated member 22 is the distance between the valley portion 22b and the mountain portion 22a on one surface of the large corrugated member 22 in the height direction, and the height direction is defined as the liner member 10. The directions are orthogonal.

コルゲートハニカム構造体1のライナー部材10とコルゲート部材20は、基材と、基材に保持された吸着剤で構成されることが好ましい。
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 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 on 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 an adsorbent. Examples of the fiber base material include a paper base material containing cellulose fiber as a main component and a plastic base material containing synthetic fiber as a main component. Of these, a paper base material containing cellulose fibers as a main component is preferable.
In addition, "as a main component" means that the ratio to the whole base material is 50% by mass or more.

紙基材は、典型的には、セルロース繊維を含むパルプから構成される。セルロース繊維を含むパルプとしては、木材パルプ、非木材パルプ等が挙げられる。木材パルプとしては、針葉樹パルプ、広葉樹パルプ等が挙げられる。非木材パルプとしては、麻パルプ、ケナフパルプ、竹パルプ等が挙げられる。 The paper substrate is typically composed of pulp containing cellulose fibers. Examples of pulp containing cellulose fibers include wood pulp and non-wood pulp. Examples of wood pulp include softwood pulp and hardwood pulp. Examples of non-wood pulp include hemp pulp, kenaf pulp, bamboo pulp and the like.

木材パルプは、蒸解工程および/または漂白工程を経たものであってもよい。一般に、木材パルプは、原料の木材からセルロース以外の成分を除去するために、種々の蒸解工程や漂白工程を施して用いられる。本発明において、蒸解工程や漂白工程は特に限定されず、適宜、公知の方法を用いることができる。
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 undergone a cooking step and / or a bleaching step. Generally, wood pulp is used by subjecting it to various cooking steps and bleaching steps in order to remove components other than cellulose from the raw wood. In the present invention, the cooking step and the bleaching step are not particularly limited, and a known method can be used as appropriate.
These pulps may be used alone or in combination of two or more.

紙基材は、セルロース繊維以外の他の繊維をさらに含んでいてもよい。他の繊維としては、例えばレーヨン繊維、ポリエチレン繊維、ポリプロピレン繊維、ポリエステル繊維等の合成繊維、ガラス繊維、セラミックス繊維、鉱物繊維等の無機繊維、動物繊維等が挙げられる。
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 the cellulose fibers. Examples of other fibers include synthetic fibers such as rayon fiber, polyethylene fiber, polypropylene fiber and polyester fiber, inorganic fiber such as glass fiber, ceramic fiber and mineral fiber, and animal fiber.
The paper substrate may contain an internal chemical such as a sizing agent, a paper strength enhancer, a colorant, a preservative, and a flame retardant. As the internal medicine, a known one can be used.

プラスチック基材としては、例えばレーヨン繊維、ポリエチレン繊維、ポリプロピレン繊維、ポリエステル繊維等の合成繊維の一種以上を主成分とするものが挙げられる。
基材の坪量は、10〜500g/mであることが好ましく、10〜400g/mであることがより好ましく、10〜300g/m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 base material include those containing one or more synthetic fibers such as rayon fiber, polyethylene fiber, polypropylene fiber, and polyester fiber as the main component.
The basis weight of the base material is preferably 10 to 500 g / m 2, more preferably from 10 to 400 g / m 2, further preferably 10 to 300 g / m 2.
The fiber base material is preferably obtained by the papermaking method.

基材に保持させる吸着剤としては、粒状、粉末、繊維状等の活性炭、モルデナイト、フェリエライト、モレキュラーシーブス等のゼオライト、シリカゲル、アルミナゲル等の公知の吸着剤が挙げられる。これらの吸着剤には、除去対象成分と反応する薬品(例えばアンモニアやホルムアルデヒドと反応する化合物)を担持させてもよい。また除去対象成分と反応する薬品を基材に直接担持させてもよい。
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 retained on the substrate include activated carbon such as granular, powder and fibrous, zeolites such as mordenite, ferrierite and molecular sieves, silica gel and known adsorbents such as alumina gel. These adsorbents may carry a chemical that reacts with the component to be removed (for example, a compound that reacts with ammonia or formaldehyde). Further, a chemical that reacts with the component to be removed may be directly supported on the base material.
The adsorbent to be retained on the substrate may be retained inside the substrate, adhered to the surface, or may be present both inside and on the surface.
The adsorbent to be retained on the substrate may be internally added at the time of papermaking, or may be applied or impregnated after papermaking.

コルゲートハニカム構造体1の製造方法に特に限定はないが、ライナー部材10に小コルゲート部材21を接着させた片段ボール(以下「小片段ボール」という。)と、ライナー部材10に大コルゲート部材22を接着させた片段ボール(以下「大片段ボール」という。)を積層し接着して製造することが好ましい。 The method for manufacturing the corrugated honeycomb structure 1 is not particularly limited, but a single corrugated cardboard (hereinafter referred to as “small corrugated cardboard”) in which a small corrugated cardboard member 21 is bonded to a liner member 10 and a large corrugated cardboard 22 are bonded to the liner member 10. It is preferable to stack and bond the corrugated cardboard (hereinafter referred to as "large corrugated cardboard").

また、大片段ボールは、一対の大コルゲート部材22の山部22a同士を接着し、一対のライナー部材10の間に一対の大コルゲート部材22が、一対の大コルゲート部材22の山部22a同士が接着した状態で挟まれた構造体(以下「X構造フルート」という。本実施形態では、図2のX構造フルート70)とし、このX構造フルート70と小片段ボールと積層接着することが好ましい。 Further, in the large piece corrugated cardboard, the mountain portions 22a of the pair of large corrugated members 22 are adhered to each other, the pair of large corrugated members 22 are adhered between the pair of liner members 10, and the mountain portions 22a of the pair of large corrugated members 22 are adhered to each other. It is preferable to form a structure sandwiched in the above-mentioned state (hereinafter referred to as “X-structured flute”; in the present embodiment, the X-structured flute 70 in FIG. 2), and to laminate and bond the X-structured flute 70 and the small piece of corrugated cardboard.

X構造フルート70と小片段ボールと積層接着する場合、X構造フルート70のライナー部材10と小片段ボールのライナー部材10とが重ねられてもよい。また、X構造フルート70のライナー部材10に小片段ボールの小コルゲート部材21側を接着し、この小片段ボールのライナー部材10と他の小片段ボールのライナー部材10とが重なるようにして、積層接着してもよい。
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。
In the case of laminating and adhering the X-structured flute 70 and the small piece of corrugated cardboard, the liner member 10 of the X-structured flute 70 and the liner member 10 of the small piece of corrugated board may be overlapped. Further, the small corrugated board member 21 side of the small corrugated cardboard is adhered to the liner member 10 of the X-structured flute 70, and the liner member 10 of the small corrugated cardboard and the liner member 10 of another small corrugated cardboard are laminated and bonded so as to overlap each other. May be good.
That is, when the corrugated honeycomb structure 1 is manufactured by laminating and adhering a small piece of corrugated cardboard and an X-structured flute, a portion in which a liner member 10 constituting one piece of corrugated board exists alone and two pieces constituting a pair of piece of corrugated board are formed. A portion existing in a state of being overlapped with the liner member 10 of the above is formed.

図3は、本発明の一実施形態に係るエアフィルタの模式的な断面図である。図3のエアフィルタは、図1、2に示したコルゲートハニカム構造体1のセル30に多孔質の充填剤50が複数充填され、コルゲートハニカム構造体1の第1の面61と第2の面62に、各々通気性シート71と通気性シート72が配置されている。 FIG. 3 is a schematic cross-sectional view of the air filter according to the embodiment of the present invention. In the air filter of FIG. 3, a plurality of porous fillers 50 are filled in the cells 30 of the corrugated honeycomb structure 1 shown in FIGS. 1 and 2, and the first surface 61 and the second surface of the corrugated honeycomb structure 1 are filled. A breathable sheet 71 and a breathable sheet 72 are arranged in 62, respectively.

充填剤50は多孔質であることにより、悪臭等の除去成分を吸着する能力を持っている。充填剤50としては、粒状、粉末、繊維状等の活性炭、モルデナイト、フェリエライト、モレキュラーシーブス等のゼオライト、シリカゲル、アルミナゲル等が挙げられる。中でも活性炭が好ましく、粒状活性炭がより好ましく、球状または略球状の活性炭が特に好ましい。 Since the filler 50 is porous, it has an ability to adsorb components for removing malodor and the like. Examples of the filler 50 include activated carbon such as granular, powder, and fibrous, zeolite such as mordenite, ferrierite, and molecular sieves, silica gel, and alumina gel. Of these, activated carbon is preferable, granular activated carbon is more preferable, and spherical or substantially spherical activated carbon is particularly preferable.

充填剤50には、無機酸等の除去対象成分と反応する薬品を担持させてもよい。
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 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 it is spherical or substantially spherical, it is easy to fill the cell 30, and an appropriate gap is formed between the liner member 10 and the corrugated member 20 that demarcate the cell 30, and it is easy to secure ventilation.

充填剤50の平均粒子径は、500〜10000μmであることが好ましく、1000〜5000μmであることがより好ましい。なお、平均粒子径は、JIS K1474(活性炭試験方法―平均粒径測定法)に準拠し、質量平均粒径法にて測定される。 The average particle size of the filler 50 is preferably 500 to 10000 μm, more preferably 1000 to 5000 μm. The average particle size is measured by the mass average particle size method in accordance with JIS K1474 (activated carbon test method-average particle size measurement method).

充填剤50の比表面積は、600〜2200m/gであることが好ましい。比表面積は、窒素ガス吸着法で測定したBET比表面積である。
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 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.
When the specific surface area of the filler 50 is at least the above-mentioned preferable lower limit value, it is easy to exhibit the adsorption performance of malodorous components and the like. Further, when 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 can be easily maintained.

最小径セル31の個数(100%)に占める充填剤50が充填された最小径セル31の個数の割合(充填率)は、50%以下であることが好ましく、25%以下であることがより好ましく、10%以下であることがさらに好ましい。
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 minimum diameter cells 31 filled with the filler 50 to the number of the minimum diameter cells 31 (100%) is preferably 50% or less, and more preferably 25% or less. It is preferably 10% or less, and more preferably 10% or less.
When the filling rate of the minimum diameter cell 31 is not more than the preferable upper limit value, it is easy to secure the air permeability.
In order to make the filling rate of the minimum diameter cell 31 equal to or less than the preferable upper limit value, the ratio of the filler 50 having a diameter smaller than that of the minimum diameter inscribed circle 41 to the entire filler 50 may be reduced.
The lower limit of the filling rate of the minimum diameter cell 31 may be 0%. That is, the minimum diameter cell 31 may not be filled with the filler 50.

一方、大径セル(本実施形態の場合第1大径セル32及び第2大径セル33)の個数(100%)に占める充填剤50が充填された大径セルの個数の割合(充填率)は、25〜100%であることが好ましく、50〜100%であることがより好ましく、75〜100%であることがさらに好ましい。
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 (filling rate) of the number of large-diameter cells filled with the filler 50 to the number (100%) of the large-diameter cells (first large-diameter cell 32 and second large-diameter cell 33 in the case of the present embodiment). ) Is preferably 25 to 100%, more preferably 50 to 100%, and even more preferably 75 to 100%.
When the filling rate of the large-diameter cell is equal to or higher than the preferable lower limit value, the filler 50 can easily increase the adsorption efficiency and sustainability. If the filling rate of the large-diameter cell is equal to or less than the preferable upper limit, the filling operation is easy.
In determining the filling factor, regardless of the size of the filler 50, a cell filled with at least one is regarded as a filled cell.

図3では、充填剤50として球状の小充填剤51と小充填剤51より大きい大充填剤52とを充填した例を模式的に示している。
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 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. This makes it difficult for the small filler 51 to fill the minimum diameter cell 31.
Even if the diameter of the filler 50 is larger than the minimum diameter inscribed circle 41, the minimum diameter cell 31 may be filled with the filler 50 or the like as fragments due to cracking or the like.

充填剤50はセル30に充填されているので、何れの直径も、第2大径内接円43より小さい。また、大充填剤52の直径は、第1大径内接円42より大きいことが好ましい。これにより、大充填剤52が第2大径セル33に充填されやすくなり、第2大径セル33の充填率を向上させることができる。 Since the filler 50 is filled in the cell 30, any diameter is smaller than the second large diameter inscribed circle 43. Further, the diameter of the large filler 52 is preferably larger than that of the first large diameter inscribed circle 42. As a result, the large-diameter cell 52 can be easily filled with the large-diameter cell 33, and the filling rate of the second large-diameter cell 33 can be improved.

通気性シート71、通気性シート72は、不織布やメッシュクロス等の通気性材料で構成されている。不織布やメッシュクロス等を構成する材料としては、レーヨン、ポリエステル、ナイロン等が挙げられる。
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 breathable sheet 71 and the breathable sheet 72 are made of a breathable material such as a non-woven fabric or a mesh cloth. Examples of the material constituting the non-woven fabric, mesh cloth, etc. include rayon, polyester, nylon, and the like.
The breathable sheet 71 and the breathable sheet 72 are arranged so as to be adhered to the first surface 61 value and the second surface 62 of the corrugated honeycomb structure 1, respectively.
By locating the breathable sheet 71 and the breathable sheet 72, it is possible to prevent the filler 50 from falling off from the air filter. In addition, dust and the like can be removed from the gas passing through the air filter.

なお、図1、2では、X構造フルート70を有するコルゲートハニカム構造体1としたが、X構造フルート70を有することは必ずしも必須ではない。例えば大きさの異なる三種類の片段ボールを用いて組み合わせて積層した構成でもよい。
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。
In FIGS. 1 and 2, the corrugated honeycomb structure 1 having the X-structured flute 70 is used, but it is not always necessary to have the X-structured flute 70. For example, three types of corrugated cardboard of different sizes may be used in combination and laminated.
Further, 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.
Further, the shape of the cell 30 is not particularly limited.
Further, in FIGS. 1 and 2, the large corrugated member 22 and the small corrugated member 21 have different configurations in both pitch and height, but a plurality of types of corrugated members 20 having different pitch and height are used. May be good.
Further, as long as the cell 30 can include cells having different sizes, the corrugated member 20 may be of one type. For example, a plurality of X-structured flutes created using one type of corrugated cardboard may be laminated.
Further, 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.

[実施例1]
坪量50g/m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/m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 liner base paper is made of glass fiber mixed paper with a basis weight of 50 g / m 2 (manufactured by Oji F-Tex) and impregnated with an adsorbent dispersion containing activated carbon, an inorganic adsorbent, a chemical adsorbent, etc. at a ratio of 200 g / L. It was made into a member.
Glass fiber mixed paper (manufactured by Oji Ftex) with a basis weight of 50 g / m 2 is used as corrugated base paper, and is impregnated with an adsorbent dispersion containing activated carbon, an inorganic adsorbent, a chemical adsorbent, etc. at a ratio of 200 g / L. It was used as a base material for corrugated use.
After the corrugated base material was corrugated to form a corrugated member, a liner member and a laminated piece corrugated cardboard were formed. Two types of corrugated cardboard, small corrugated cardboard and large corrugated cardboard, with different heights and pitches were prepared. For the small corrugated cardboard, a small corrugated member having a pitch of 4.9 mm and a height of 2 mm was used, and for the large corrugated cardboard, a large corrugated member having a pitch of 5.9 mm and a height of 3 mm was used.

得られた大片段ボール2枚を、大コルゲート部材の稜線同士を合わせて、ライナー部材が両外側となるように接着し、その両外側のライナー部材に、各々小片段ボールのコルゲート部材を接着した積層体を得た。この積層体を複数重ね、図1に示したのと同等のコルゲートハニカム構造体を得た。なお、各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。また、コルゲートハニカム構造の厚さ(セルの深さ方向の長さ)は、15mmとした。 The two obtained large pieces of corrugated cardboard are bonded together so that the ridgelines of the large corrugated cardboards are aligned with each other so that the liner members are on both outer sides, and the corrugated members of the small pieces of corrugated board are bonded to the liner members on both outer sides. Got A plurality of these laminated bodies were stacked to obtain a corrugated honeycomb structure equivalent to that shown in FIG. In addition, each piece of corrugated cardboard was laminated by aligning the ridge line direction of the corrugated member. The thickness of the corrugated honeycomb structure (length in the depth direction of the cell) was set to 15 mm.

得られたコルゲートハニカム構造体の一方の面に通気性シートを接着し、他方の面から、充填剤として、大阪ガスケミカル(株)製薬品担持球状活性炭((平均粒径2mm、BET比表面積930m/g)の23gを充填した。その後、他方の面にも通気性シートを接着し、実施例1のエアフィルタを得た。
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 breathable sheet was adhered to one surface of the obtained corrugated honeycomb structure, and from the other surface, a chemical-supported spherical activated carbon manufactured by Osaka Gas Chemical Co., Ltd. ((average particle size 2 mm, BET specific surface area 930 m)) was used as a filler. It was filled with 23 g of 2 / g). Then, a breathable sheet was also adhered to the other surface to obtain an air filter of Example 1.
As the breathable sheet, a polyester mesh (opening 1 mm) was used.

[比較例1]
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 piece corrugated cardboard used in Example 1 had a structure in which a plurality of liner members and corrugated members were bonded to each other and laminated. In addition, a plurality of large pieces of corrugated cardboard were laminated so that the ridgeline directions of the corrugated members were aligned.

[圧力損失評価]
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, it is set in a wind tunnel device, and each line of 0.5 m / s, 1.0 m / s, 1.5 m / s, and 2.0 m / s. The pressure loss at high speed was measured.
The results are shown in Table 1.

Figure 2020145345
Figure 2020145345

表1に示すように、実施例1のエアフィルタが、圧力損失の点で比較例1と比べて優れることがわかる。
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 side 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 minimum diameter cell was hardly filled with the filler and the filling rate did not exceed 50%. Further, it was confirmed that most of the large-diameter cells could be filled with the filler, and the filling rate was at least 25% or more. In particular, 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 confirmed that the filler such as activated carbon could be filled while securing the cell in which the filler was not filled and the gas could easily pass through and suppressing the increase in the pressure loss.

[比較例2]
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]
In Example 1, an air filter was obtained in the same manner as in Example 1 except that the spherical activated carbon was not filled.

[ホルムアルデヒド除去性能評価]
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1m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]
Employing an evaluation test based on the Chinese GB standards (GB / T 18801-2015), by the simple test of the size of the test chamber was 1 m 3, the clean air supply rate after formaldehyde loading of the air filter (CADR) and clean air Formaldehyde removal performance was evaluated by measuring the supply rate maintenance rate (CADR maintenance rate).

(初期CADRの測定)
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)
An air purifier fan equipped with the air filter obtained in Example 1 and Comparative Example 2 was set, and the air purifier was sealed in a test chamber so that the aerial concentration of formaldehyde was 1 ppm, and the air purifier was the same as the target air purifier. It is operated at a linear speed (LV) of 1.0 m / s, and the formaldehyde air concentration is measured for 60 minutes at 5-minute intervals using a formaldehyde meter http. The air supply rate (initial CADR) was measured.
The results are shown in Table 2.

(ホルムアルデヒド負荷後のCADRの測定)
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 formaldehyde loading)
Next, the air-cleaning fan equipped with the air filter obtained in Example 1 and Comparative Example 2 was set, and the filter paper on the volatilization fan was impregnated with a formaldehyde solution so that the mass of formaldehyde was 20 mg. And the volatilization fan was operated and left for 12 hours.

さらに、上記の処理を施し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(1m)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、ホルムアルデヒド20mg/枚負荷後のクリーンエア供給率(CADR)を測定した。Furthermore, an air purifier equipped with an air filter that has undergone the above treatment is set and sealed in a test room (1 m 3) so that the aerial concentration of formaldehyde is 1 ppm. It was operated at the same linear velocity (LV) of 1.0 m / s, and the formaldehyde air concentration was measured for 60 minutes at 5-minute intervals using a formaldehyde meter http. The clean air supply rate (CADR) after loading 20 mg / sheet was measured.

初期クリーンエア供給率(初期CADR)と、上記ホルムアルデヒド20mg/枚負荷後のクリーンエア供給率(CADR)との関係から、20mg負荷後のクリーンエア供給率維持率(CADR維持率)を算出した。 From the relationship between the initial clean air supply rate (initial CADR) and the clean air supply rate (CADR) after the formaldehyde 20 mg / sheet load, the clean air supply rate maintenance rate (CADR maintenance rate) after the 20 mg load was calculated.

Figure 2020145345
Figure 2020145345

表2に示すとおり、実施例1のエアフィルタは、初期だけでなく、20mg相当吸着後においても高い吸着性能を示した。 As shown in Table 2, the air filter of Example 1 showed high adsorption performance not only at the initial stage but also after adsorption equivalent to 20 mg.

本発明の活性炭等の充填剤を充填したエアフィルタは、圧力損失の上昇を抑制しながら、吸着効率や持続性を高めることができる。
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 a filler such as activated carbon of 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 malodorous components, harmful components, and the like.

1 コルゲートハニカム構造体
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 Corrugated honeycomb structure 10 Liner member 20 Corrugated member 21 Small corrugated member 22 Large corrugated member 30 Cell 31 Minimum diameter cell 32 1st large diameter cell 33 2nd large diameter cell 41 Minimum diameter inscribed circle 42 1st large diameter inscribed circle Circle 43 Second large diameter inscribed circle 50 Filler 51 Small filler 52 Large filler 61 First surface 62 Second surface 71 Breathable sheet 72 Breathable sheet

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 demarcating a plurality of cells arranged in a plane direction and a plurality of porous fillers filled in the plurality of cells are provided.
The plurality of cells consist of a plurality of minimum diameter cells and a plurality of large diameter cells.
The plurality of minimum diameter cells are the cells having the smallest diameter of the inscribed circle.
The plurality of large-diameter cells are cells in which the diameter of the inscribed circle is larger than the diameter of the inscribed circle of the plurality of minimum-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.
An air filter characterized in that the ratio of the number of large-diameter cells filled with the filler to the number of large-diameter 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 minimum 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 such that a plurality of liner members and a plurality of corrugated members are bonded to each other.
The plurality of liner members are linear when observed from a direction perpendicular to the plane direction.
The plurality of corrugated members have a wavy shape in which peaks and valleys repeat along the direction in which the liner member extends when observed from a direction perpendicular to the plane 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 one or both of the heights and 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 or more corrugated members in which the mountain portions are directly adhered to each other without interposing the liner member. 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 the adsorbent is held in 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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Citations (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2001096166A (en) * 1999-09-30 2001-04-10 Mitsubishi Paper Mills Ltd Photocatalyst component
JP2002210328A (en) * 2001-01-18 2002-07-30 Mitsubishi Heavy Ind Ltd Exhaust gas treatment method and treatment apparatus
JP2003047649A (en) * 2001-05-29 2003-02-18 Sanei Service Kk Deodorizing filter
CN1499997A (en) * 2001-04-07 2004-05-26 3M Combination filter for filtering fluids
JP2005304844A (en) * 2004-04-22 2005-11-04 Mitsubishi Paper Mills Ltd Composite deodorization filter
JP2006231324A (en) * 2005-01-26 2006-09-07 Nichias Corp Composition for cleaning ozone containing exhaust gas, and filter for cleaning the same
JP2008212448A (en) * 2007-03-06 2008-09-18 Toray Ind Inc Air cleaning filter
JP2012183534A (en) * 2005-12-20 2012-09-27 Mitsubishi Chemicals Corp Adsorbing sheet, adsorbing element, method for manufacturing the same, and use of the same
JP2013078540A (en) * 2011-10-05 2013-05-02 Sharp Corp Filter and air purifier

Family Cites Families (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE10153283A1 (en) * 2001-10-29 2003-05-15 Emitec Emissionstechnologie Heat-resistant filter layer, filter body and process for its production
CN2826248Y (en) * 2005-04-11 2006-10-11 亚翔工程股份有限公司 Air filtering structure
CN100479902C (en) * 2006-05-09 2009-04-22 亚翔系统集成科技(苏州)有限公司 Chemical filtering net
DE102008025593A1 (en) * 2008-05-28 2009-12-03 Emitec Gesellschaft Für Emissionstechnologie Mbh Metallic honeycomb body with defined joints
JP2013132637A (en) * 2011-12-27 2013-07-08 Toyota Boshoku Corp Filter and air conditioner
BR112017007297B1 (en) * 2014-10-10 2022-02-01 Baldwin Filters, Inc Method for providing reinforcement of a packet filtering medium
CN106925051A (en) * 2017-03-15 2017-07-07 广西华原过滤系统股份有限公司 A kind of honeycomb fashion filters core

Patent Citations (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2001096166A (en) * 1999-09-30 2001-04-10 Mitsubishi Paper Mills Ltd Photocatalyst component
JP2002210328A (en) * 2001-01-18 2002-07-30 Mitsubishi Heavy Ind Ltd Exhaust gas treatment method and treatment apparatus
CN1499997A (en) * 2001-04-07 2004-05-26 3M Combination filter for filtering fluids
JP2003047649A (en) * 2001-05-29 2003-02-18 Sanei Service Kk Deodorizing filter
JP2005304844A (en) * 2004-04-22 2005-11-04 Mitsubishi Paper Mills Ltd Composite deodorization filter
JP2006231324A (en) * 2005-01-26 2006-09-07 Nichias Corp Composition for cleaning ozone containing exhaust gas, and filter for cleaning the same
JP2012183534A (en) * 2005-12-20 2012-09-27 Mitsubishi Chemicals Corp Adsorbing sheet, adsorbing element, method for manufacturing the same, and use of the same
JP2008212448A (en) * 2007-03-06 2008-09-18 Toray Ind Inc Air cleaning filter
JP2013078540A (en) * 2011-10-05 2013-05-02 Sharp Corp Filter and air purifier

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