CN114618261A - Filter membrane - Google Patents

Filter membrane Download PDF

Info

Publication number
CN114618261A
CN114618261A CN202011474628.7A CN202011474628A CN114618261A CN 114618261 A CN114618261 A CN 114618261A CN 202011474628 A CN202011474628 A CN 202011474628A CN 114618261 A CN114618261 A CN 114618261A
Authority
CN
China
Prior art keywords
honeycomb structure
honeycomb
filtration membrane
sheet base
thickness direction
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
CN202011474628.7A
Other languages
Chinese (zh)
Inventor
田中健太郎
宫崎一希
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Oji Holdings Corp
Original Assignee
Oji Holdings Corp
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Oji Holdings Corp filed Critical Oji Holdings Corp
Priority to CN202011474628.7A priority Critical patent/CN114618261A/en
Priority to JP2021184329A priority patent/JP2022094310A/en
Priority to KR1020210174150A priority patent/KR20220085012A/en
Publication of CN114618261A publication Critical patent/CN114618261A/en
Pending legal-status Critical Current

Links

Images

Classifications

    • 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
    • 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
    • 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
    • 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
    • B01D46/2422—Mounting of the body within a housing
    • 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
    • B01D46/54—Particle separators, e.g. dust precipitators, using ultra-fine filter sheets or diaphragms
    • B01D46/543—Particle separators, e.g. dust precipitators, using ultra-fine filter sheets or diaphragms using membranes
    • 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
    • B01D53/22—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 diffusion
    • B01D53/228—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 diffusion characterised by specific membranes
    • 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
    • B01D53/34—Chemical or biological purification of waste gases
    • B01D53/38—Removing components of undefined structure
    • 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
    • B01D53/34—Chemical or biological purification of waste gases
    • B01D53/74—General processes for purification of waste gases; Apparatus or devices specially adapted therefor
    • B01D53/81—Solid phase processes
    • B01D53/82—Solid phase processes with stationary reactants
    • 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
    • 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
    • B01D2253/106—Silica or silicates
    • 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
    • B01D2253/106—Silica or silicates
    • B01D2253/108—Zeolites
    • 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
    • B01D2253/112—Metals or metal compounds not provided for in B01D2253/104 or B01D2253/106
    • B01D2253/1124—Metal oxides
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D2257/00—Components to be removed
    • B01D2257/90—Odorous compounds not provided for in groups B01D2257/00 - B01D2257/708
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D2257/00—Components to be removed
    • B01D2257/91—Bacteria; Microorganisms

Landscapes

  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Engineering & Computer Science (AREA)
  • Analytical Chemistry (AREA)
  • General Chemical & Material Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Environmental & Geological Engineering (AREA)
  • Health & Medical Sciences (AREA)
  • Biomedical Technology (AREA)
  • Physics & Mathematics (AREA)
  • Geometry (AREA)
  • Filtering Materials (AREA)

Abstract

The invention provides a filtering membrane which can improve the contact efficiency of gas such as air when the gas passes through. The filtration membrane (1) has a plurality of honeycomb structures (2) having a thickness of 3mm or less and stacked in the thickness direction, each honeycomb structure (2) has a sheet base (4), the sheet base (4) includes a plurality of spaces (3) arranged along a plane perpendicular to the thickness direction and partitioned from each other, and the spaces (3) of each honeycomb structure (2) are arranged so that a part of the sheet base (4) of another honeycomb structure (2) adjacent in the thickness direction overlaps with a part of the spaces (3).

Description

Filter membrane
Technical Field
The present invention relates to a filtration membrane used for purposes such as deodorization.
Background
For example, in an air cleaner or the like, as a filter membrane used for the purpose of deodorization or the like, there is known a honeycomb structure including a plurality of partitioned cells (spaces) by alternately stacking a plurality of spacer members and corrugated members (see, for example, patent documents 1 to 4). The honeycomb structure is formed using, for example, paper on which a chemical such as an adsorbent is supported, and purifies air by adsorbing malodorous components and the like while the air to be treated passes through cells that become flow paths. The honeycomb structure can effectively remove the removal target component by sufficiently contacting air while the air passes through the cells. Therefore, in the conventional honeycomb structure for a filtration membrane, the contact area with the air passing through the cells is increased by increasing the length of the cells, and the thickness (length of the cells) is generally about 10mm to 30 mm.
Documents of the prior art
Patent document
Patent document 1: japanese laid-open patent publication No. 2007-125466
Patent document 2: japanese patent laid-open publication No. 2017-074309
Patent document 3: japanese patent No. 3719356
Patent document 4: japanese patent No. 4040889
Disclosure of Invention
Problems to be solved by the invention
In the honeycomb structure described in patent documents 1 to 4, as shown in fig. 17, the cells 101 extend almost straight in the thickness direction of the honeycomb structure 100, and the cells 101 are a structure through which gas easily passes. Therefore, the honeycomb structure 100 has a low contact efficiency with air, and the one-pass removal efficiency when used as a filtration membrane is limited. As a method for improving the contact efficiency with air of the honeycomb structure 100, there is a method of increasing the number of cells 101 per unit area, but this method has a disadvantage of increasing the amount of chemicals such as paper and an adsorbent used for the honeycomb structure 100.
The present invention has been made in view of the above problems, and an object of the present invention is to provide a filtration membrane capable of improving the efficiency of contact with a gas such as air when the gas passes through the filtration membrane.
Means for solving the problems
As a result of earnest studies, the present inventors have found that the above-mentioned problems can be solved and reached the present invention by designing the thickness of a honeycomb structure used for a filtration membrane to be thinner than that of a conventional honeycomb structure and stacking a plurality of honeycomb structures having a reduced thickness in the thickness direction to form the filtration membrane, and in this case, designing the arrangement of cells (spaces) of the plurality of honeycomb structures so that the flow of air or the like passing through the cells (spaces) of the plurality of honeycomb structures becomes turbulent. In summary, the filtration membrane of the present invention comprises the structure described in the following item 1.
Item 1. a filtration membrane having a plurality of honeycomb structures having a thickness of 3mm or less and stacked in the thickness direction, wherein,
each of the honeycomb structures has a sheet base including a plurality of spaces arranged along a plane perpendicular to the thickness direction and partitioned from each other,
the space of each of the honeycomb structures is arranged so that a part of the sheet base material of another adjacent honeycomb structure in the thickness direction overlaps with a part of the space.
The filtration membrane of the present invention preferably has a structure described in the following items 2 to 11.
The filtration membrane according to item 1, wherein the sheet base material has a plurality of gasket members extending straight in a plan view and a plurality of wavy corrugated members in which peaks and valleys are alternately connected in an extending direction of the gasket members in a plan view, and the plurality of gasket members and the plurality of corrugated members are alternately joined with the corrugated members interposed between the two gasket members.
Item 3. the filtration membrane according to item 2, wherein a direction in which the cushion member of each of the honeycomb structures extends is different from a direction in which the cushion member of the other honeycomb structure adjacent in the thickness direction extends.
Item 4. the filtration membrane according to item 3, wherein an extending direction of the cushion member of each of the honeycomb structures is different from an extending direction of the cushion member of the other honeycomb structure adjacent in the thickness direction by 90 °.
Item 5. the filtration membrane according to item 2, wherein a height and/or a pitch of the waves of the corrugated member of each of the honeycomb structures is different from a height and/or a pitch of the waves of the corrugated members of the other honeycomb structures adjacent in the thickness direction.
The filtration membrane according to any one of claims 1 to 5, wherein at least a part of the sheet base material of the honeycomb structure carries a chemical.
The filtration membrane of item 7, wherein the sheet base material of a portion of the honeycomb structures carries a different type of drug than the sheet base material of at least a portion of the other honeycomb structures.
The filtration membrane according to any one of claims 1 to 7, wherein at least a part of the space of at least a part of the honeycomb structure is filled with a filler of a porous medium.
The filtration membrane according to any one of claims 1 to 8, wherein the honeycomb structure has four or more.
The filtration membrane according to any one of claims 1 to 9, wherein the total thickness is 25mm or less.
ADVANTAGEOUS EFFECTS OF INVENTION
The filtering membrane of the invention can improve the contact efficiency of gas such as air when the gas passes through.
Drawings
Fig. 1 is an exploded perspective view of a filter membrane according to an embodiment of the present invention.
Fig. 2 is a plan view of the honeycomb structure.
Fig. 3 is a partially enlarged view of fig. 2.
Fig. 4 is a partially enlarged plan view showing a state where 2 honeycomb structures shown in fig. 1 are stacked.
Fig. 5 is a partially enlarged plan view showing a state where 2 honeycomb structures shown in fig. 1 are stacked.
Fig. 6 is a partially enlarged cross-sectional view showing a state in which 3 honeycomb structures shown in fig. 1 are stacked.
Fig. 7 is a plan view of a honeycomb structure according to a modification.
Fig. 8 is a partially enlarged cross-sectional view showing a state in which 2 honeycomb structures shown in fig. 1 and the honeycomb structure shown in fig. 7 are stacked.
Fig. 9 is a plan view of a honeycomb structure according to a modification.
Fig. 10 is a partially enlarged cross-sectional view of a state in which the honeycomb structure shown in fig. 2 and the honeycomb structure shown in fig. 9 are stacked.
Fig. 11 is a plan view of a honeycomb structure according to a modification.
Fig. 12 is a partially enlarged cross-sectional view showing a state in which the honeycomb structure shown in fig. 2 and the honeycomb structure shown in fig. 11 are stacked.
Fig. 13 is a plan view of a honeycomb structure according to a modification.
Fig. 14 is a partially enlarged cross-sectional view showing a state in which the honeycomb structure shown in fig. 2 and the honeycomb structure shown in fig. 13 are stacked.
Fig. 15A to 15D are explanatory views showing steps of manufacturing a honeycomb structure.
FIGS. 16A to 16B are graphs showing the deodorizing performance of the filtration membranes of the examples and comparative examples.
Fig. 17 is an enlarged cross-sectional view of a part of a conventional honeycomb structure.
Description of the reference numerals
1. A filtration membrane; 2. a honeycomb structure; 3. a space; 4. a sheet base material; 5. a pad member; 6. a corrugated member; 60. a peak; 61. a valley portion.
Detailed Description
Hereinafter, embodiments of the present invention will be described with reference to the drawings. Fig. 1 is an exploded perspective view of a filter membrane 1 according to an embodiment of the present invention. The filter membrane 1 is used for removing a component to be removed from a gas such as air, and is used for the purpose of deodorizing, removing foreign substances, and the like in an air cleaner, for example. The filter membrane 1 has a plurality of honeycomb structures 2. The filtration membrane 1 is formed by stacking a plurality of honeycomb structures 2 in the thickness direction (Z direction in fig. 1), and joining one surface of each of the honeycomb structures 2 adjacent in the thickness direction to each other with an adhesive or the like to integrate the plurality of honeycomb structures 2.
The honeycomb structure 2 is formed in a flat shape having a small thickness and spreading in a planar shape. The thickness (length in the Z direction in fig. 1) of the honeycomb structure 2 is 3mm or less, preferably 2mm or less, and more preferably 1.5mm or less. The honeycomb structure 2 may have a thickness, and the lower limit of the thickness is not particularly limited, but is preferably 1mm or more in view of production. As described above, the honeycomb structure 2 of the present embodiment is designed to have a smaller thickness than the conventional honeycomb structure, and the filter membrane 1 is formed by stacking a plurality of the honeycomb structures 2 having a smaller thickness, so that various effects which cannot be achieved by the filter membrane using the conventional honeycomb structure can be achieved, and details thereof will be described later.
As shown in fig. 1 to 3, the honeycomb structure 2 has a sheet base 4 having a rectangular shape in a plan view. The shape of the sheet base 4 in a plan view is not particularly limited, and various shapes can be used. The sheet base 4 includes a plurality of spaces 3 arranged along a plane (XY plane) perpendicular to the thickness direction and divided from each other. The space 3 is generally called a "cell" and is open at both upper and lower ends in the thickness direction of the sheet base 4 so as to penetrate through the sheet base 4 in the thickness direction. The space 3 serves as a flow path through which a gas such as air to be processed passes. The shape of the space 3 in a plan view is not particularly limited, and in the illustrated example, the space has a mountain shape (substantially triangular shape), but may have a quadrilateral shape, a rhomboid shape, a hexagonal shape, a circular shape, or the like. The plurality of spaces 3 are connected in a narrow interval arrangement regularly or irregularly in the longitudinal, lateral, diagonal, etc. directions in the XY plane. The plurality of spaces 3 may be the same size or different sizes. The plurality of spaces 3 may have the same shape or may be different from each other.
The sheet base 4 is formed to include a plurality of spaces 3 and to divide adjacent spaces 3 into spaces. The sheet base 4 is not particularly limited, and paper, nonwoven fabric, plastic film, or the like can be used as a raw material, but a fiber base is preferably used from the viewpoint of easily carrying a chemical such as an adsorbent. Examples of the fiber base material include a base material mainly composed of glass fibers, a paper base material mainly composed of cellulose fibers, and a plastic base material mainly composed of synthetic fibers. Among the fiber base materials, a base material containing glass fibers as a main component can be preferably used. As the substrate containing glass fibers as a main component, glass fiber mixed paper is more preferable. The phrase "as a main component" means that the proportion thereof to the entire base material is 50% by mass or more.
The paper substrate is typically comprised of a pulp containing cellulosic fibers. The pulp containing cellulose is not particularly limited, and examples thereof include wood pulp, non-wood pulp, and the like. The wood pulp is not particularly limited, and may be softwood pulp, hardwood pulp, or the like. The non-wood pulp is not particularly limited, and examples thereof include hemp pulp, kenaf pulp, and bamboo pulp. One of these pulps may be used alone, or two or more of them may be used in combination.
The wood pulp may also be subjected to a cooking process and/or a bleaching process. In general, various cooking steps and bleaching steps are applied to wood pulp in order to remove components other than cellulose from raw wood. The cooking step and the bleaching step are not particularly limited, and known methods can be appropriately used.
The paper substrate may further contain other fibers than cellulose fibers. Examples of the other fibers include synthetic fibers such as rayon, polyethylene fibers, polypropylene fibers, and polyester fibers; inorganic fibers such as glass fibers, ceramic fibers, and mineral fibers; animal fibers, and the like.
The paper substrate may further contain an internal chemical such as a sizing agent, a paper strength enhancer, a colorant, a preservative, and a flame retardant. As the chemical to be added internally, a known chemical can be used.
Examples of the plastic substrate include substrates containing one or more synthetic fibers such as rayon, polyethylene fiber, polypropylene fiber, and polyester fiber as a main component.
The mass per unit area of the sheet base 4 is not particularly limited, but is preferably 10g/m2Above 500g/m2Hereinafter, more preferably 10g/m2Above 400g/m2Hereinafter, it is more preferably 10g/m2Above 300g/m2The following.
The sheet base 4 has a plurality of cushion members 5 extending straight in a plan view and a plurality of corrugated members 6 waved in a plan view. The spacer member 5 and the corrugated member 6 are thin strip members having a width in the thickness direction of the honeycomb structure 2. The corrugated member 6 is formed by alternately connecting convex ridges 60 and concave valleys 61 in a wavy manner along the direction in which the pad member 5 extends (hereinafter referred to as "extending direction") in a plan view, and by repeatedly bending a thin strip-shaped member. The plurality of pad members 5 and the plurality of corrugated members 6 are alternately arranged so that the corrugated member 6 is sandwiched between the two pad members 5, and the sheet base material 4 is formed by bonding the tops of the crests 60 of the corrugated member 6 to one pad member 5 with, for example, an adhesive or the like, and bonding the bottoms of the troughs 61 of the corrugated member 6 to the other pad member 5 with, for example, an adhesive or the like. The space 3 is a space divided by the corrugated member 6 and the cushion member 5.
The pitch l (the length between the tops of adjacent ridges 60) and the height h (the length from the top of the ridge 60 to the bottom of the valley 61) of the waves of the corrugated member 6 constituting the sheet base 4 are equal, and the positions of the ridges 60 and the valley 61 of the corrugated member 6 are aligned in the extending direction of the cushion member 5. The corrugated member 6 may have different wave pitches l and heights h, and the peak portions 60 and the valley portions 61 of the corrugated member 60 may be shifted in position in the extending direction of the cushion member 5.
The honeycomb structure 2 preferably has a chemical supported on the sheet base 4 in addition to the sheet base 4. Examples of the chemical include a chemical (adsorbent) having a function of adsorbing malodorous components, a chemical (antibacterial agent, antifungal agent) having an antibacterial/antifungal function, and a chemical (ozonolysis agent) having a function of decomposing ozone.
The adsorbent is not particularly limited, and examples thereof include activated carbon; zeolites such as mordenite, ferrierite, molecular sieves and the like; silica gel; alumina gel and the like.
The antibacterial agent and the antifungal agent are not particularly limited, and known antibacterial agents and antifungal agents such as silver-containing antibacterial agents can be mentioned.
The ozonolysis agent is not particularly limited, and known ozonolysis agents such as a manganese catalyst type ozonolysis agent, a copper-manganese catalyst type ozonolysis agent, and an activated carbon type ozonolysis agent can be mentioned.
The drug is not limited to these, and various other known drugs can be used. The chemical may be in various forms such as powder, granule, and fiber, and the method of supporting the chemical on the sheet base 4 may be to hold the chemical inside the sheet base 4, to attach the chemical to the surface of the sheet base 4, to apply an immersion liquid containing the chemical to the sheet base 4, or to immerse the sheet base 4 in the immersion liquid. By carrying the chemical on the sheet base 4, the air purification function such as deodorization can be efficiently achieved.
The honeycomb structure 2 may further include a frame member for covering and protecting the sheet base 4 from the periphery.
The extending direction of the spacer member 5 of each of the plurality of honeycomb structures 2 forming the filter membrane 1 is directed in a direction different from the extending direction of the spacer member 5 of another honeycomb structure 2 adjacent in the thickness direction. In short, the extending directions of the cushion members 5 of two honeycomb structural bodies 2 adjacent in the thickness direction intersect at a predetermined angle.
Here, the other honeycomb structures 2 adjacent in the thickness direction refer to two honeycomb structures 2 adjacent on the upper side and the lower side in the thickness direction among the honeycomb structures 2 other than the honeycomb structure 2 at the upper end and the lower end in the thickness direction of the filter membrane 1. On the other hand, the honeycomb structure 2 at the upper end in the thickness direction of the filter membrane 1 means one honeycomb structure 2 adjacent to the lower side in the thickness direction, and the honeycomb structure 2 at the lower end in the thickness direction of the filter membrane 1 means one honeycomb structure 2 adjacent to the upper side in the thickness direction.
The predetermined angle is not particularly limited, and is 90 ° in the illustrated example. In short, in the present embodiment, the extending direction of the spacer member 5 of each honeycomb structure 2 is directed in a direction different from the extending direction of the spacer member 5 of another honeycomb structure 2 adjacent in the thickness direction by 90 °, and the plurality of honeycomb structures 2 are stacked while being rotated by 90 ° in the XY plane every other honeycomb structure 2.
Thus, the spaces 3 of the respective honeycomb structures 2 are arranged so that a part of the sheet base 4 of another honeycomb structure 2 adjacent in the thickness direction overlaps with a part of the spaces 3. That is, fig. 4 is a plan view showing, for example, a part of the second honeycomb structure 2 and the third honeycomb structure 2 from the upper side in fig. 1 in an enlarged manner, and the space 3 of one (third honeycomb structure 2 located on the lower side) and the space 3 of the other (second honeycomb structure 2 located on the upper side) do not completely coincide with each other. A part of the sheet base material 4 (the spacer member 5 and the corrugated member 6) of the other (the second on the upper side) honeycomb structure 2 enters the range of the space 3 of the one (the third on the lower side) honeycomb structure 2, and the sheet base material 4 (the spacer member 5 and the corrugated member 6) of the other (the second on the upper side) honeycomb structure 2 exists so as to block the air passing through the space 3 from flowing smoothly with respect to the space 3 of the one (the third on the lower side) honeycomb structure 2.
Fig. 5 is a plan view showing, for example, a part of the first honeycomb structure 2 and the second honeycomb structure 2 in fig. 1 in an enlarged manner in a state of being overlapped from the upper side, and the space 3 of one (second honeycomb structure 2 located on the lower side) is not completely matched with the space 3 of the other (first honeycomb structure 2 located on the upper side) in the same manner. A part of the sheet base material 4 (the spacer member 5 and the corrugated member 6) of the other (first upper) honeycomb structural body 2 enters the range of the space 3 of the one (second lower) honeycomb structural body 2, and the sheet base material 4 (the spacer member 5 and the corrugated member 6) of the other (first upper) honeycomb structural body 2 exists so as to block the air passing through the space 3 from flowing smoothly with respect to the space 3 of the one (second lower) honeycomb structural body 2.
When a gas to be treated, such as air, passes through the filtration membrane 1, the gas passes through the spaces 3 of the plurality of honeycomb structures 2 forming the filtration membrane 1. Here, as shown in fig. 6, when gas flows from the space 3 of one honeycomb structure 2 to the space 3 of the other honeycomb structure 2 between the two adjacent honeycomb structures 2, the smooth flow of the gas is blocked by the sheet base material 4 (the cushion member 5 and the corrugated member 6) of the other honeycomb structure 2, and the flow of the gas is disturbed to be turbulent. When the flow of the gas becomes turbulent, the contact efficiency of the gas with respect to the honeycomb structure 2 is improved as compared with a structure in which the cells (spaces) 101 extend almost straight in the thickness direction of the honeycomb structure 100 as in the conventional art shown in fig. 15. Further, when gas flows from the space 3 of one honeycomb structure 2 to the space 3 of the other honeycomb structure 2 between the adjacent two honeycomb structures 2, the gas collides with the sheet base material 4 (the cushion member 5 and the corrugated member 6) of the other honeycomb structure 2, whereby the contact area of the gas in the honeycomb structures 2 is also increased. Therefore, the gas removal target component is effectively adsorbed by the honeycomb structure 2, and therefore, the one-pass removal efficiency of the filtration membrane 1 can be improved.
Even if the pitch l and the height h of the waves of the corrugated members 6 of the plurality of honeycomb structures 2 forming the filter membrane 1 are the same, the shapes in plan view thereof do not necessarily have to be completely the same. As shown in fig. 7, the positions of the crests 60 and troughs 61 of the corrugated member 6 may be shifted in the extending direction of the gasket member 5 in comparison with, for example, another honeycomb structure 2 shown in fig. 2 with respect to at least a part of the honeycomb structure 2, and the planar shape may be substantially the same but slightly different.
Fig. 8 is a plan view of a state in which two honeycomb structures 2 having the shapes shown in fig. 2 are stacked so that the extending direction of the spacer member 5 is changed by 90 degrees, and then one honeycomb structure 2 having the shapes shown in fig. 7 is stacked so that the extending direction of the spacer member 5 is changed by 90 degrees. Further, a plan view of a state in which three honeycomb structures 2 having the shape shown in fig. 2 are stacked so that the extending direction of the spacer member 5 is changed by 90 degrees one by one is roughly as shown in fig. 4 and 5. When a plurality of honeycomb structures 2 are stacked in the thickness direction, the spaces 3 and the sheet base 4 in fig. 8 are intricately staggered, and the entire structure of the spaces 3 is extremely complicated in a plan view. Therefore, the flow of gas such as air passing through the filter membrane 1 is likely to be turbulent. This can further improve the contact efficiency of the honeycomb structure 2 with the gas.
In the present embodiment, the extending direction of the spacer member 5 of each of the plurality of honeycomb structures 2 forming the filtration membrane 1 is directed in a direction different by 90 ° from the extending direction of the spacer member 5 of another honeycomb structure 2 adjacent in the thickness direction. However, the angle does not necessarily need to be 90 °, and may be any angle, and among these, 15 ° to 90 °, and most preferably 90 °, is preferable.
Fig. 10 is a partially enlarged plan view showing a state where the honeycomb structure 2 having the shape shown in fig. 9 is superimposed on the upper side of the honeycomb structure 2 having the shape shown in fig. 2. In the honeycomb structural body 2 having the shape shown in fig. 9, the extending direction of the cushion member 5 is directed in a direction different by 45 ° from the extending direction of the honeycomb structural body 2 having the shape shown in fig. 2. In this modification, when two honeycomb structures 2 are stacked, the space 3 of one honeycomb structure 2 does not completely coincide with the space 3 of the other honeycomb structure 2. A part of the sheet base material 4 (the spacer member 5 and the corrugated member 6) of the other honeycomb structure 2 enters the range of the space 3 of the one honeycomb structure 2, and the sheet base material 4 (the spacer member 5 and the corrugated member 6) of the other honeycomb structure 2 exists so as to block the air passing through the space 3 of the one honeycomb structure 2 from flowing smoothly. Note that the same applies to the case where the honeycomb structure 2 having the shape shown in fig. 2 is superimposed on the upper side of the honeycomb structure 2 having the shape shown in fig. 9, but illustration thereof is omitted. Thus, by alternately stacking a plurality of filter membranes 1 formed on the honeycomb structure 2 having the shape shown in fig. 2 and the honeycomb structure 2 having the shape shown in fig. 9, the flow of gas such as air passing through the filter membranes 1 becomes turbulent, and the contact efficiency of the honeycomb structure 2 with gas can be improved.
In addition to the honeycomb structure having the shape shown in fig. 2 and the honeycomb structure 2 having the shape shown in fig. 9, a honeycomb structure 2 in which the extending direction of the spacer member 5 is further oriented in a direction different by 45 ° from the honeycomb structure 2 having the shape shown in fig. 9 (a honeycomb structure 2 in which the extending direction of the spacer member 5 is oriented in a direction different by 90 ° from the honeycomb structure 2 having the shape shown in fig. 2, and a second honeycomb structure 2 from the upper side in fig. 1) may be used, and a plurality of filter membranes 1 forming a modification may be alternately stacked on the honeycomb structures 2.
In the plurality of honeycomb structures 2 forming the filtration membrane 1, the sheet base material 4 preferably supports a chemical on at least a part of the honeycomb structures 2, and more preferably supports a plurality of different chemicals on the sheet base material 4 in a part or all of the honeycomb structures 2. For example, the sheet substrate 4 of one of the honeycomb structures 2 among the plurality of honeycomb structures 2 may carry an antibacterial agent and/or a mildewproofing agent, the sheet substrate 4 of another one of the honeycomb structures 2 may carry an ozone decomposing agent, and the sheet substrate 4 of at least a remaining one of the honeycomb structures 2 may carry an adsorbent. Thus, one filter membrane 1 can exhibit various performances. The types of drugs to be carried are not limited to 3, but may be 2, 4 or more, and different types of drugs may be carried on the sheet base material 4 of each honeycomb structure 2.
The filter membrane 1 may have a filler (not shown) of a porous medium in addition to the plurality of honeycomb structures 2. The filler is filled in at least a part of the space 3 of at least a part of the honeycomb structure 2. The filler is a porous medium, thereby exerting the performance of adsorbing the malodorous components and the like. Examples of the filler include granular, powdery, fibrous and the like activated carbon; zeolites such as mordenite, ferrierite, molecular sieves and the like; silica gel; alumina gel, and the like. Among these, activated carbon is preferable, and spherical or substantially spherical granular activated carbon is more preferable from the viewpoint of easy filling into the space 3. The filler may also contain a known chemical that reacts with a component to be removed, such as ammonia or aldehydes.
The total thickness (length in the Z direction in fig. 1) of the filtration membrane 1 is not particularly limited, and can be appropriately set according to the application of the filtration membrane 1, and is preferably set to 4mm or more.
The number of the honeycomb structures 2 forming the filter membrane 1 is not particularly limited as long as it is a plurality, and can be appropriately set in accordance with the total thickness of the filter membrane 1 and the thickness of the honeycomb structure 2, and is preferably 4 or more, more preferably 6 or more, and still more preferably 10 or more, from the viewpoint of favorably making the flow of air or the like passing through the filter membrane 1 turbulent.
The filter membrane 1 of the present embodiment described above is formed of a plurality of honeycomb structures 2, and each honeycomb structure 2 is laminated such that a part of the sheet base material 4 of another honeycomb structure 2 adjacent to the space 3 through which a gas such as air passes in the thickness direction overlaps with a part of the space 3. Therefore, when the gas passes through the filtration membrane 1 of the present embodiment, when the gas flows from the space 3 of one honeycomb structure 2 to the space 3 of the other honeycomb structure 2 between the two adjacent honeycomb structures 2, the flow of the gas is disturbed and disturbed to be turbulent by the sheet base material 4 of the other honeycomb structure 2. This improves the contact efficiency of the honeycomb structure 2 with air. Further, when air flows between two adjacent honeycomb structures 2 from the space 3 of one honeycomb structure 2 to the space 3 of the other honeycomb structure 2, the air collides with the sheet base material 4 of the other honeycomb structure 2, whereby the contact area of the air in the honeycomb structures 2 is also increased. As described above, with the filtration membrane 1 of the present embodiment, the removal target component of the gas passing through the filtration membrane 1 is effectively adsorbed by the honeycomb structure 2, and therefore, the once-through removal efficiency of the filtration membrane 1 can be improved.
In addition, in the filtration membrane 1 of the present embodiment, in order to improve the contact efficiency between the honeycomb structure 2 and the gas, only a plurality of honeycomb structures 2 having a thickness of 3mm or less, which are extremely thin as compared with the conventional honeycomb structure, are stacked, and therefore the amount of a raw material such as paper or a chemical used for the plurality of honeycomb structures 2 is not increased as compared with the conventional honeycomb structure. This enables the formation of a high-performance filtration membrane 1 without an additional increase.
Even if the number of spaces per unit area is increased in the conventional honeycomb structure, the contact efficiency can be achieved to the same extent as that of the filtration membrane 1 of the present embodiment, but in this case, the pressure loss when the gas passes through the filtration membrane is also greatly increased. In contrast, the filtration membrane 1 of the present embodiment can reduce the pressure loss as compared with a conventional honeycomb structure having the same performance.
Further, since the filter membrane 1 of the present embodiment is formed not by a single honeycomb structure but by a plurality of honeycomb structures 2, different types of chemicals can be carried on different honeycomb structures 2. Thus, various effects can be exhibited by one filtration membrane 1.
In the filtration membrane 1 of the present embodiment, the sheet base material 4 of each honeycomb structure 2 is composed of the plurality of spacer members 5 and the plurality of corrugated members 6, and the extending direction of the spacer member 5 is different by 90 ° from the extending direction of the spacer member 5 of another honeycomb structure 2 adjacent in the thickness direction, whereby the effect of making the flow of the gas passing through the filtration membrane 1 turbulent can be achieved. Therefore, when a plurality of honeycomb structures 2 are stacked to form the filtration membrane 1, only one kind of honeycomb structures 2 having substantially the same shape is prepared, and the extending direction of the spacer member 5 is changed by rotating the honeycomb structures 2 by 90 ° every other honeycomb structure, and therefore, the filtration membrane 1 can be easily formed.
While the embodiments of the present invention have been described above, the specific embodiments of the present invention are not limited to the above-described embodiments, and various modifications can be made without departing from the scope of the invention.
In the above embodiment, the extending direction of the spacer member 5 is made different for each honeycomb structure 2 of the plurality of honeycomb structures 2 forming the filter membrane 1 from the extending direction of the spacer member 5 of another honeycomb structure 2 adjacent in the thickness direction. Thus, the spaces 3 of the respective honeycomb structures 2 are arranged so that a part of the sheet base 4 of another honeycomb structure 2 adjacent in the thickness direction overlaps with a part of the spaces 3, and as a result, the flow of the gas passing through the filter membrane 1 becomes turbulent. The method of making the flow of the gas passing through the filter membrane 1 turbulent is not limited to this, and as a modification, for example, the height h and/or pitch 1 of the wave of the corrugated member 6 of each honeycomb structure 2 may be different from the height h and/or pitch l of the corrugated member 6 of another honeycomb structure 2 adjacent in the thickness direction.
Fig. 12 is a partially enlarged plan view showing a state where the honeycomb structure 2 having the shape shown in fig. 11 is superimposed on the upper side of the honeycomb structure 2 having the shape shown in fig. 2. In the honeycomb structural body 2 having the shape shown in fig. 11, the pitch l' of the waves of the corrugated member 6 is different from the pitch l and is smaller than the pitch l, as compared with the honeycomb structural body 2 having the shape shown in fig. 2. In this modification, when two honeycomb structures 2 are superimposed, the space 3 of one honeycomb structure 2 does not completely coincide with the space 3 of the other honeycomb structure 2. A part of the sheet base material 4 (the spacer member 5 and the corrugated member 6) of the other honeycomb structure 2 enters the range of the space 3 of the one honeycomb structure 2, and the sheet base material 4 (the spacer member 5 and the corrugated member 6) of the other honeycomb structure 2 exists so as to block the air passing through the space 3 of the one honeycomb structure 2 from flowing smoothly. Note that the same applies to the case where the honeycomb structure 2 having the shape shown in fig. 2 is superimposed on the upper side of the honeycomb structure 2 having the shape shown in fig. 11, but illustration thereof is omitted. Thus, by alternately stacking a plurality of filter membranes 1 formed by the honeycomb structure 2 having the shape shown in fig. 2 and the honeycomb structure 2 having the shape shown in fig. 11, the flow of gas such as air passing through the filter membranes 1 becomes turbulent, and the contact efficiency of the honeycomb structure 2 with the gas can be improved.
When a plurality of filtration membranes 1 are formed by alternately stacking the honeycomb structure 2 having the shape shown in fig. 2 and the honeycomb structure 2 having the shape shown in fig. 11, the position of the spacer member 5 of each honeycomb structure 2 may be completely matched with the position of the spacer member 5 of another honeycomb structure 2 adjacent in the thickness direction in a plan view, or may be shifted in the XY plane in a direction perpendicular to the extending direction of the spacer member 5.
Further, 3 or more kinds of honeycomb structures 2 having different wave pitches of the corrugated member 6 may be prepared, and a plurality of the 3 or more kinds of honeycomb structures 2 may be alternately stacked to form the filter membranes 1.
Fig. 14 is a partially enlarged plan view showing a state where the honeycomb structure 2 having the shape shown in fig. 13 is superimposed on the upper side of the honeycomb structure 2 having the shape shown in fig. 2. In the honeycomb structure 2 having the shape shown in fig. 13, the height h' of the waves of the corrugated member 6 is different from the height h and the height h is smaller than that of the honeycomb structure 2 having the shape shown in fig. 2. In this modification, when two honeycomb structures are superimposed, the space 3 of one honeycomb structure 2 does not completely coincide with the space 3 of the other honeycomb structure 2. A part of the sheet base material 4 (the spacer member 5 and the corrugated member 6) of the other honeycomb structure 2 enters the range of the space 3 of the one honeycomb structure 2, and the sheet base material 4 (the spacer member 5 and the corrugated member 6) of the other honeycomb structure 2 exists so as to block the air passing through the space 3 of the one honeycomb structure 2 from flowing smoothly. Note that the same applies to the case where the honeycomb structure 2 having the shape shown in fig. 2 is superimposed on the upper side of the honeycomb structure 2 having the shape shown in fig. 13, but illustration thereof is omitted. Thus, by alternately stacking a plurality of filter membranes 1 formed by the honeycomb structure 2 having the shape shown in fig. 2 and the honeycomb structure 2 having the shape shown in fig. 13, the flow of gas such as air passing through the filter membranes 1 becomes turbulent, and the contact efficiency of the honeycomb structure 2 with the gas can be improved.
When a plurality of filtration membranes 1 are formed by alternately stacking the honeycomb structure 2 having the shape shown in fig. 2 and the honeycomb structure 2 having the shape shown in fig. 13, the spacer member 5 of each honeycomb structure 2 may partially overlap with the spacer member 5 of another honeycomb structure 2 adjacent in the thickness direction in a plan view, or may be offset in a direction perpendicular to the extending direction of the spacer member 5.
Further, 3 or more kinds of honeycomb structures 2 having different wave heights of the corrugated member 6 may be prepared, and a plurality of filtration membranes 1 may be formed by alternately stacking the 3 or more kinds of honeycomb structures 2.
Further, it is also possible to prepare 2 or more kinds of honeycomb structures 2 having different wave heights and pitches of the corrugated members 6, and alternately stack a plurality of the 2 or more kinds of honeycomb structures 2 to form the filter membranes 1.
As another modification of the method of making the flow of gas passing through the filter membrane 1 turbulent, for example, the crests 60 and troughs 61 of the corrugated structure 6 of each honeycomb structure 2 may be offset in the extending direction of the spacer member 5 with respect to the crests 60 and troughs 61 of the corrugated members 6 of another honeycomb structure 2 adjacent in the thickness direction, but the illustration thereof is omitted.
In the above-described embodiment and any modification, the spaces 3 of the respective honeycomb structures 2 do not necessarily have to overlap a part of the sheet base material 4 of another honeycomb structure 2 adjacent in the thickness direction with a part of the spaces 3 with respect to all the spaces 3, and even if this is not satisfied with a part of the spaces 3, the flow of the gas passing through the separator 1 can be made turbulent.
In the above embodiment, the honeycomb structure 2 has a structure (corrugated honeycomb structure) including the plurality of spacer members 5 and the plurality of corrugated members 6, and as another modification, the honeycomb structure 2 may be a honeycomb structure other than the corrugated honeycomb structure as long as the plurality of spaces 3 are connected in a narrow interval arrangement regularly or irregularly in the longitudinal, lateral, diagonal, etc. directions in the XY plane.
Examples
The following examples of the present invention are shown. However, the present invention is not limited to the following examples.
(1) Examples of the embodiments
[ production of Honeycomb Structure A containing silica gel ]
Referring to FIGS. 15A to 15D, first, a mass per unit area of 50g/m is used2The sheet for a spacer member and the sheet for a corrugated member shown in FIG. 15A were produced from the glass fiber mixed paper (product of Wangzi F-TEX Co., Ltd.) as a base paper. The corrugated sheet was obtained by corrugating base paper so that pitch l was 5.9mm and height h was 3.1 mm. Then, the corrugated member sheet and the spacer member sheet are bonded to each other to produce a single-faced corrugated sheet.
Next, 30 single-faced corrugated sheets shown in fig. 15A were prepared, and as shown in fig. 15B, a laminated body was produced by laminating and laminating 30 single-faced corrugated sheets. In the lamination, the crest line of the corrugated member sheet of one of the adjacent single-faced corrugated sheets is made to correspond to the back surface (the surface opposite to the surface to which the corrugated member sheet is bonded) of the liner member sheet of the other single-faced corrugated sheet, and the corrugated member sheets are bonded to each other. The adhesive is vinyl acetate emulsion.
Next, as shown in fig. 15C, the obtained laminate was sliced into a plurality of pieces so as to have a thickness of 1 mm. Thus, as shown in fig. 15D, a sheet base material constituting the honeycomb structure was produced. Slicing is performed in such a manner that the skin of vegetables and fruits is removed (peeled).
Subsequently, the obtained plurality of sheet substrates were immersed in an adsorbent dispersion containing 21g/L of silica gel, 3g/L of an aldehyde absorbent and 3g/L of an acrylic binder, and then each sheet substrate was dried. Thereby, a plurality of honeycomb structures a were produced.
[ production of activated carbon-containing Honeycomb Structure B ]
A plurality of sheet substrates having a thickness of 1mm constituting the honeycomb structure were produced by the same procedure as in the above-described honeycomb structure a (see fig. 15D). The obtained plurality of sheet substrates were immersed in an adsorbent dispersion containing 20g/L of activated carbon and 3g/L of an acrylic binder, and then each sheet substrate was dried. In this way, a plurality of honeycomb structures B were produced.
[ production of filtration Membrane ]
Each of 5 honeycomb structures a and 5 honeycomb structures B was alternately laminated and bonded in the thickness direction. In the lamination, the extending direction of the spacer member of the honeycomb structure a and the extending direction of the spacer member of the honeycomb structure B are different by 90 °, and in short, the honeycomb structure a and the honeycomb structure B are laminated while changing the orientation so that the extending direction of the spacer member is orthogonal to the extending direction of the upper and lower honeycomb structures adjacent to each other in the thickness direction. Thus, a filtration membrane having a thickness of 10mm, in which 10 honeycomb structures were stacked, was obtained (example). The amounts of the adsorbents in the filtration membranes of the examples were 3.3g of activated carbon, 3.1g of silica gel and 0.4g of aldehyde absorbent.
(2) Comparative example 1
A laminate was obtained by the same procedure as in example (see fig. 15B). Then, the laminate was sliced into a thickness of 10mm, and then immersed in an adsorbent dispersion containing 21g/L of silica gel, 3g/L of an aldehyde absorbent and 3g/L of an acrylic binder, followed by drying. Thus, a filtration membrane having a thickness of 10mm was obtained (comparative example 1). The amounts of the adsorbents in the filtration membrane of comparative example 1 were 0g of activated carbon, 4.2g of silica gel, and 0.6g of an aldehyde absorbent.
(3) Comparative example 2
A laminate was obtained by the same procedure as in example (see fig. 15B). Then, the laminate was sliced into a thickness of 10mm, and then immersed in an adsorbent dispersion containing 20g/L of activated carbon and 3g/L of an acrylic binder, followed by drying. Thus, a filtration membrane having a thickness of 10mm was obtained (comparative example 2). The amounts of the adsorbents in the filtration membrane of comparative example 2 were 4.4g of activated carbon, 0g of silica gel, and 0g of aldehyde absorbent.
(4) Evaluation of
[ deodorant Property ]
Malodorous gases (acetaldehyde and toluene) were injected into the acrylic resin chamber. At the time of starting injection, the malodorous gas is injected so that the concentration thereof becomes 15. + -.1 ppm. After the initial concentration of malodorous gas was confirmed, the blower was attached to each of the filtration membranes of examples and comparative examples 1 and 2, and the blower was operated. The time-dependent change in the malodorous gas concentration in the chamber was measured under the following measurement conditions, with the start of the operation of the blower set to 0 minute. Fig. 16A to 16B show the measurement results.
< test conditions >
Chamber volume 1m3
The size of the filtering membrane is 100mm multiplied by 10mm thick
Air volume of 0.9m3Min (═ 1.5m/sec face wind speed)
Gas concentration measurement gas detection tube (available from GASTEC corporation, aldehyde detection tube: 92L, toluene detection tube: 122L)
As shown in fig. 16A, it is understood that the filtration membrane of the example has the same acetaldehyde removal efficiency as the filtration membrane of comparative example 1, and is very superior to the acetaldehyde removal efficiency of the filtration membrane of comparative example 2. As shown in fig. 16B, the filtration membrane of the example and the filtration membrane of comparative example 2 showed the same toluene removal efficiency, and were very superior to the toluene removal efficiency of the filtration membrane 1 of comparative example 1.
From the above results, the filtration membrane of the example has both functions of the filtration membrane of comparative example 1 and the filtration membrane of comparative example 2, and the above function of the filtration membrane of the example can be achieved with a thickness smaller than 20mm which is the total value of the thickness of the filtration membrane of comparative example 1 and the thickness of the filtration membrane of comparative example 2.

Claims (10)

1. A filtration membrane, wherein,
has a plurality of honeycomb structures having a thickness of 3mm or less and stacked in the thickness direction,
each of the honeycomb structures has a sheet base material including a plurality of spaces arranged along a plane perpendicular to the thickness direction and partitioned from each other,
the space of each of the honeycomb structures is arranged so that a part of the sheet base material of another adjacent honeycomb structure in the thickness direction overlaps with a part of the space.
2. The filtration membrane of claim 1,
the sheet base material has a plurality of pad members extending straight in a plan view and a plurality of wavy corrugated members in which crests and troughs are alternately connected in a direction in which the pad members extend in a plan view, and the plurality of pad members and the plurality of corrugated members are alternately joined to each other so as to sandwich the corrugated members between the two pad members.
3. The filtration membrane of claim 2,
the honeycomb structure has a structure in which the direction in which the spacer member extends is different from the direction in which the spacer member extends of another honeycomb structure adjacent in the thickness direction.
4. The filtration membrane of claim 3,
the extending direction of the spacer member of each of the honeycomb structures is different from the extending direction of the spacer member of the other honeycomb structure adjacent in the thickness direction by 90 °.
5. The filtration membrane of claim 2,
the height and/or pitch of the wave of the corrugated member of each honeycomb structure is different from the height and/or pitch of the wave of the corrugated member of another honeycomb structure adjacent in the thickness direction.
6. The filtration membrane according to any one of claims 1 to 5, wherein,
at least a part of the sheet base material of the honeycomb structure carries a chemical.
7. The filtration membrane of claim 6,
a drug of a different type from that of the other at least a part of the sheet base material of the honeycomb structure is carried on a part of the sheet base material of the honeycomb structure.
8. The filtration membrane according to any one of claims 1 to 7, wherein,
at least a part of the space of at least a part of the honeycomb structure is filled with a filler of a porous medium.
9. The filtration membrane according to any one of claims 1 to 8, wherein,
there are four or more of the honeycomb structures.
10. The filtration membrane according to any one of claims 1 to 9,
the total thickness is less than 25 mm.
CN202011474628.7A 2020-12-14 2020-12-14 Filter membrane Pending CN114618261A (en)

Priority Applications (3)

Application Number Priority Date Filing Date Title
CN202011474628.7A CN114618261A (en) 2020-12-14 2020-12-14 Filter membrane
JP2021184329A JP2022094310A (en) 2020-12-14 2021-11-11 filter
KR1020210174150A KR20220085012A (en) 2020-12-14 2021-12-07 Filter

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN202011474628.7A CN114618261A (en) 2020-12-14 2020-12-14 Filter membrane

Publications (1)

Publication Number Publication Date
CN114618261A true CN114618261A (en) 2022-06-14

Family

ID=81897126

Family Applications (1)

Application Number Title Priority Date Filing Date
CN202011474628.7A Pending CN114618261A (en) 2020-12-14 2020-12-14 Filter membrane

Country Status (1)

Country Link
CN (1) CN114618261A (en)

Similar Documents

Publication Publication Date Title
CA2304156C (en) Filter for gases
AU2005301258B2 (en) Gathered filter media for an air filter and method of making same
US7112255B2 (en) Thermobondable filter medium and border frame and method of making same
KR102331811B1 (en) Filtration media, pleated media pack, filter cartridge, and methods for manufacturing
US8673148B2 (en) Multifiltration cartridge filtration apparatus
US20110005394A1 (en) Media for removal of organic compounds
JPH06339611A (en) Filter
US9492775B2 (en) Air filtration media, media constructions and methods
US6227383B1 (en) Filtering material and process for the production thereof, and adsorption filter produced from said filtering material
CN214862342U (en) Filter membrane
KR20220085012A (en) Filter
CN114618261A (en) Filter membrane
CN214075611U (en) Gas filter
JP3504715B2 (en) Suction element
JP7393352B2 (en) air filter
JPH0783812B2 (en) Activated carbon fiber-containing paper having protrusions and laminate thereof
CN111097243A (en) Filter with separator sheet comprising special folds
US20230051258A1 (en) Filter media having surface topography and comprising fibrillated fibers
JPS6355971B2 (en)
CN212283308U (en) Inclined hole crossing honeycomb filter screen
WO2023228963A1 (en) Honeycomb structure sheet, laminate, and method for producing same
WO2005011841A1 (en) Water-resistant filters
JP4885048B2 (en) Manufacturing method of deodorizing air filter
JPH09290116A (en) Air filter of low pressure loss
JP2002361344A (en) Honeycombed structure and honeycomb functional material

Legal Events

Date Code Title Description
PB01 Publication
PB01 Publication
SE01 Entry into force of request for substantive examination
SE01 Entry into force of request for substantive examination