WO2013190905A1 - フィルタ用の濾材およびその製造方法 - Google Patents
フィルタ用の濾材およびその製造方法 Download PDFInfo
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- WO2013190905A1 WO2013190905A1 PCT/JP2013/062024 JP2013062024W WO2013190905A1 WO 2013190905 A1 WO2013190905 A1 WO 2013190905A1 JP 2013062024 W JP2013062024 W JP 2013062024W WO 2013190905 A1 WO2013190905 A1 WO 2013190905A1
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F02—COMBUSTION ENGINES; HOT-GAS OR COMBUSTION-PRODUCT ENGINE PLANTS
- F02M—SUPPLYING COMBUSTION ENGINES IN GENERAL WITH COMBUSTIBLE MIXTURES OR CONSTITUENTS THEREOF
- F02M35/00—Combustion-air cleaners, air intakes, intake silencers, or induction systems specially adapted for, or arranged on, internal-combustion engines
- F02M35/02—Air cleaners
- F02M35/024—Air cleaners using filters, e.g. moistened
- F02M35/02441—Materials or structure of filter elements, e.g. foams
- F02M35/0245—Pleated, folded, corrugated filter elements, e.g. made of paper
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D39/00—Filtering material for liquid or gaseous fluids
- B01D39/14—Other self-supporting filtering material ; Other filtering material
- B01D39/16—Other self-supporting filtering material ; Other filtering material of organic material, e.g. synthetic fibres
- B01D39/1607—Other self-supporting filtering material ; Other filtering material of organic material, e.g. synthetic fibres the material being fibrous
- B01D39/1623—Other self-supporting filtering material ; Other filtering material of organic material, e.g. synthetic fibres the material being fibrous of synthetic origin
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D39/00—Filtering material for liquid or gaseous fluids
- B01D39/14—Other self-supporting filtering material ; Other filtering material
- B01D39/16—Other self-supporting filtering material ; Other filtering material of organic material, e.g. synthetic fibres
- B01D39/18—Other self-supporting filtering material ; Other filtering material of organic material, e.g. synthetic fibres the material being cellulose or derivatives thereof
-
- 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
- B01D46/52—Particle separators, e.g. dust precipitators, using filters embodying folded corrugated or wound sheet material
- B01D46/521—Particle separators, e.g. dust precipitators, using filters embodying folded corrugated or wound sheet material using folded, pleated material
-
- 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
- B01D46/56—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours with multiple filtering elements, characterised by their mutual disposition
- B01D46/62—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours with multiple filtering elements, characterised by their mutual disposition connected in series
-
- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21F—PAPER-MAKING MACHINES; METHODS OF PRODUCING PAPER THEREON
- D21F11/00—Processes for making continuous lengths of paper, or of cardboard, or of wet web for fibre board production, on paper-making machines
- D21F11/02—Processes for making continuous lengths of paper, or of cardboard, or of wet web for fibre board production, on paper-making machines of the Fourdrinier type
- D21F11/04—Processes for making continuous lengths of paper, or of cardboard, or of wet web for fibre board production, on paper-making machines of the Fourdrinier type paper or board consisting on two or more layers
-
- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21F—PAPER-MAKING MACHINES; METHODS OF PRODUCING PAPER THEREON
- D21F11/00—Processes for making continuous lengths of paper, or of cardboard, or of wet web for fibre board production, on paper-making machines
- D21F11/14—Making cellulose wadding, filter or blotting paper
-
- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21H—PULP COMPOSITIONS; PREPARATION THEREOF NOT COVERED BY SUBCLASSES D21C OR D21D; IMPREGNATING OR COATING OF PAPER; TREATMENT OF FINISHED PAPER NOT COVERED BY CLASS B31 OR SUBCLASS D21G; PAPER NOT OTHERWISE PROVIDED FOR
- D21H11/00—Pulp or paper, comprising cellulose or lignocellulose fibres of natural origin only
- D21H11/02—Chemical or chemomechanical or chemothermomechanical pulp
-
- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21H—PULP COMPOSITIONS; PREPARATION THEREOF NOT COVERED BY SUBCLASSES D21C OR D21D; IMPREGNATING OR COATING OF PAPER; TREATMENT OF FINISHED PAPER NOT COVERED BY CLASS B31 OR SUBCLASS D21G; PAPER NOT OTHERWISE PROVIDED FOR
- D21H13/00—Pulp or paper, comprising synthetic cellulose or non-cellulose fibres or web-forming material
- D21H13/10—Organic non-cellulose fibres
- D21H13/20—Organic non-cellulose fibres from macromolecular compounds obtained otherwise than by reactions only involving carbon-to-carbon unsaturated bonds
- D21H13/24—Polyesters
-
- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21H—PULP COMPOSITIONS; PREPARATION THEREOF NOT COVERED BY SUBCLASSES D21C OR D21D; IMPREGNATING OR COATING OF PAPER; TREATMENT OF FINISHED PAPER NOT COVERED BY CLASS B31 OR SUBCLASS D21G; PAPER NOT OTHERWISE PROVIDED FOR
- D21H15/00—Pulp or paper, comprising fibres or web-forming material characterised by features other than their chemical constitution
- D21H15/02—Pulp or paper, comprising fibres or web-forming material characterised by features other than their chemical constitution characterised by configuration
-
- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21H—PULP COMPOSITIONS; PREPARATION THEREOF NOT COVERED BY SUBCLASSES D21C OR D21D; IMPREGNATING OR COATING OF PAPER; TREATMENT OF FINISHED PAPER NOT COVERED BY CLASS B31 OR SUBCLASS D21G; PAPER NOT OTHERWISE PROVIDED FOR
- D21H21/00—Non-fibrous material added to the pulp, characterised by its function, form or properties; Paper-impregnating or coating material, characterised by its function, form or properties
- D21H21/50—Non-fibrous material added to the pulp, characterised by its function, form or properties; Paper-impregnating or coating material, characterised by its function, form or properties characterised by form
- D21H21/52—Additives of definite length or shape
-
- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21H—PULP COMPOSITIONS; PREPARATION THEREOF NOT COVERED BY SUBCLASSES D21C OR D21D; IMPREGNATING OR COATING OF PAPER; TREATMENT OF FINISHED PAPER NOT COVERED BY CLASS B31 OR SUBCLASS D21G; PAPER NOT OTHERWISE PROVIDED FOR
- D21H27/00—Special paper not otherwise provided for, e.g. made by multi-step processes
- D21H27/08—Filter paper
-
- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21H—PULP COMPOSITIONS; PREPARATION THEREOF NOT COVERED BY SUBCLASSES D21C OR D21D; IMPREGNATING OR COATING OF PAPER; TREATMENT OF FINISHED PAPER NOT COVERED BY CLASS B31 OR SUBCLASS D21G; PAPER NOT OTHERWISE PROVIDED FOR
- D21H27/00—Special paper not otherwise provided for, e.g. made by multi-step processes
- D21H27/30—Multi-ply
-
- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21H—PULP COMPOSITIONS; PREPARATION THEREOF NOT COVERED BY SUBCLASSES D21C OR D21D; IMPREGNATING OR COATING OF PAPER; TREATMENT OF FINISHED PAPER NOT COVERED BY CLASS B31 OR SUBCLASS D21G; PAPER NOT OTHERWISE PROVIDED FOR
- D21H27/00—Special paper not otherwise provided for, e.g. made by multi-step processes
- D21H27/30—Multi-ply
- D21H27/38—Multi-ply at least one of the sheets having a fibrous composition differing from that of other sheets
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F02—COMBUSTION ENGINES; HOT-GAS OR COMBUSTION-PRODUCT ENGINE PLANTS
- F02M—SUPPLYING COMBUSTION ENGINES IN GENERAL WITH COMBUSTIBLE MIXTURES OR CONSTITUENTS THEREOF
- F02M35/00—Combustion-air cleaners, air intakes, intake silencers, or induction systems specially adapted for, or arranged on, internal-combustion engines
- F02M35/02—Air cleaners
- F02M35/024—Air cleaners using filters, e.g. moistened
- F02M35/02408—Manufacturing filter elements
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2239/00—Aspects relating to filtering material for liquid or gaseous fluids
- B01D2239/06—Filter cloth, e.g. knitted, woven non-woven; self-supported material
- B01D2239/0604—Arrangement of the fibres in the filtering material
- B01D2239/064—The fibres being mixed
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2239/00—Aspects relating to filtering material for liquid or gaseous fluids
- B01D2239/06—Filter cloth, e.g. knitted, woven non-woven; self-supported material
- B01D2239/065—More than one layer present in the filtering material
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2239/00—Aspects relating to filtering material for liquid or gaseous fluids
- B01D2239/12—Special parameters characterising the filtering material
- B01D2239/1208—Porosity
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2239/00—Aspects relating to filtering material for liquid or gaseous fluids
- B01D2239/12—Special parameters characterising the filtering material
- B01D2239/1233—Fibre diameter
Definitions
- the present invention relates to a filter medium used for a filter such as an air cleaner of an automobile internal combustion engine, and more particularly to an improvement of a filter medium manufactured by wet paper making using natural fibers such as pulp and linter and chemical fibers such as polyester and rayon. .
- a filter medium for an air cleaner of an internal combustion engine for automobiles is generally made of a filter paper mainly composed of natural fibers such as pulp and linter, and the filter paper is housed in a case in the form of many folds.
- a filter paper is generally of a single layer, but in order to extend the life of the filter medium, as shown in the explanatory diagram of FIG.
- a composite filter medium having a two-layer structure in which an upper layer 22 made of a nonwoven fabric or filter paper having a relatively low density is bonded to the surface is provided for practical use.
- FIG. 10 is explanatory drawing which represented the density thru
- Patent Document 1 an upper layer paper raw material and a lower layer paper raw material are used, and the upper layer and the lower layer are supplied by feeding them onto the paper machine wire so that both are partially mixed.
- a production method for obtaining a composite filter paper having a continuous density gradient between these layers has been proposed.
- Patent Document 1 discloses that the upper layer papermaking raw material and the lower layer papermaking raw material have different blending ratios of linter fiber and rayon fiber, but the same fiber is used in this way. Only by changing the blending ratio using, good characteristics cannot always be obtained.
- the dust performance for relatively large dust particles for example, the test is performed with 7 ⁇ m particles
- the carbon performance for very small carbon particles for example, about 0.5 ⁇ m of soot
- An object of the present invention is to provide a filter medium that achieves both a high capture efficiency and a long life by using a manufacturing method as disclosed in Patent Document 1.
- the present invention is a filter medium for a filter made by using a first papermaking raw material for an upper layer and a second papermaking raw material for a lower layer so as to have a continuous density gradient from the upper layer to the lower layer.
- the first papermaking raw material and the second papermaking raw material include natural fibers and chemical fibers,
- the compounding ratio of the chemical fiber in the first papermaking raw material is higher than the compounding ratio of the chemical fiber in the second papermaking raw material,
- the thickness of the chemical fiber in the first papermaking raw material is thicker than the thickness of the chemical fiber in the second papermaking raw material,
- the basis weight is 60 to 250 g / m 2 .
- the method for producing the filter medium for the filter of the present invention includes: Preparing a first papermaking raw material containing natural fibers and chemical fibers, and a second papermaking raw material containing natural fibers and chemical fibers;
- the mixing ratio of the chemical fiber in the first papermaking raw material is higher than the mixing ratio of the chemical fiber in the second papermaking raw material
- the thickness of the chemical fiber in the first papermaking raw material is thicker than the thickness of the chemical fiber in the second papermaking raw material
- the first papermaking raw material includes natural fibers such as pulp and linter and chemical fibers such as polyester and rayon
- the second papermaking raw material similarly includes natural fibers and chemical fibers.
- the natural fiber in the first papermaking raw material and the natural fiber in the second papermaking raw material are not necessarily the same type, and similarly, the chemical fiber in the first papermaking raw material and the chemical fiber in the second papermaking raw material are the same. It is not limited to the kind.
- FIG. 1 is an explanatory view showing a production method for papermaking the filter medium of the present invention, which is not particularly different from the method described in Patent Document 1. That is, the first papermaking raw material 1 and the second papermaking raw material 2 are supplied from separate head boxes (not shown) to the wire part of the papermaking machine including the wire feed drum 3 and the wire 4. On the downstream side, the two papermaking raw materials 1 and 2 are partially mixed and placed on the wire 4 in a state where no clear interface exists. Thereby, the filter medium in which the blending ratio of the two papermaking raw materials 1 and 2 is continuously changed between the upper surface and the lower surface is obtained.
- upper layer and lower layer in the present invention mean the upstream layer and the downstream layer with respect to the flow of fluid to be filtered (for example, the flow of air in the case of a filter medium for an air cleaner).
- the upper and lower sides at the time of papermaking are not limited to this.
- FIG. 2 is an explanatory diagram of the filter medium of the present invention, and is an explanatory diagram schematically showing the density or pore size of each layer by the size of the holes, as in FIG. 10 and FIG. As shown, there is no interface between the two layers, and the density or pore size changes continuously. Therefore, basically, clogging at the interface hardly occurs.
- the upper layer has more fibers and the lower layer has more chemical fibers, and the lower layer has a dust performance with respect to relatively large dust particles (for example, the test is performed with 7 ⁇ m particles) and very small carbon particles (for example, the capture efficiency and the lifetime (period until clogging) are compatible at a higher level with respect to both carbon performance with respect to soot of about 0.5 ⁇ m.
- the compounding ratio of the chemical fiber in the first papermaking raw material is 10 to 80% (weight%, the same applies hereinafter), and the thickness of the fiber is 10%.
- the compounding ratio of the chemical fiber in the second papermaking raw material is 60% or less, and the thickness of the fiber is 3 to 20 ⁇ m.
- the compounding ratio of the chemical fiber in the first papermaking raw material is preferably 10 to 80%.
- the lower layer needs to have a higher density than the upper layer to ensure a density gradient, for example, it is necessary to increase the ratio of natural fibers so that it can be easily pleated in the subsequent process as an air cleaner element.
- the compounding ratio of the chemical fiber in the raw material is preferably 60% or less.
- the fiber diameter of the chemical fiber is preferably in the range of 10 to 30 ⁇ m for the upper layer and 3 to 20 ⁇ m for the lower layer because the thicker the fiber, the greater the effect of securing voids and lowering the density.
- the basis weight of the base paper has a high correlation with paper strength (strength) and thickness, as shown in FIG. 3, since the required strength as a filter for example air cleaner element is not obtained in less than 60 g / m 2, 60 g / M 2 or more is desirable. However, if it exceeds 250 g / m 2 , the strength is strong, but as shown in FIG. 4, it exceeds a certain thickness, and is necessary when pleated and accommodated in a case as a filter (for example, an air cleaner element).
- the area of the filter medium cannot be secured sufficiently (that is, the bulk of the filter medium becomes excessive), and the thickness is excessive and the ventilation resistance increases, so that it is preferably 250 g / m 2 or less.
- the first papermaking raw material and the second papermaking raw material are contained in a basis weight ratio of 2: 8 to 6: 4.
- the basis weight ratio between the upper layer and the lower layer is, as shown in FIG. 5, the filtration performance (indicated by DHC in the figure: DHC) and the rigidity of the filter medium. Correlation is high.
- the proportion of the low-density layer on the upstream side increases, the life of the dust performance improves (life), but when the proportion of the high-density material on the downstream side decreases too much, the rigidity of the filter medium decreases, Adhesion of the filter medium and the like occur, and the performance as a filter is likely to deteriorate (life reduction and efficiency reduction). Therefore, in consideration of both, a ratio of 2: 8 to 6: 4 that balances dust performance and rigidity is desirable.
- the thickness of the filter medium is in the range of 0.4 to 1.5 mm.
- the thickness of the filter medium has a high correlation with the filtration area and the ventilation resistance. The thinner the filter medium, the larger the filtration area can be secured in the same filter, and the ventilation resistance can be reduced. It is desirable that However, at least 0.4 mm is necessary in terms of strength.
- the density of the filter medium is in the range of 0.1 to 0.5 g / cm 3 .
- the density of the filter medium is highly correlated with the filtration performance. As shown in FIG. 7, the lower the density, the longer the life until clogging, but the lower the efficiency. A range of 1 to 0.5 g / cm 3 is desirable.
- a filter medium capable of widely filtering various sizes of particles from fine particles such as exhaust carbon to coarse dust particles having a large particle size and having a long life until clogging. Can do.
- the first papermaking material constituting the upper layer was blended with 40% mercerized pulp as natural fiber and 60% PET (polyethylene terephthalate) fiber with a fiber diameter of 18 ⁇ m as chemical fiber. A thing was used.
- As the second papermaking material constituting the lower layer 35% of mercerized pulp and 60% of ordinary pulp not converted to mercerized were mixed as natural fibers, and 5% of PET fibers having a diameter of 9 ⁇ m as chemical fibers were blended. A thing was used.
- the mercerized pulp in which the fibers are curled by alkali treatment is bulky and has a lower density than the pulp, and conversely, the pulp is superior in strength to the mercerized pulp.
- a filter medium having a continuous density gradient was made by the wet papermaking method as shown in FIG.
- the supply amount of each raw material was adjusted so that the total basis weight would be 120 g / m 2 and the basis weight ratio between the first papermaking raw material and the second papermaking raw material would be 4: 6.
- the filter medium thus obtained had a thickness (thickness not calendared) of 0.95 mm, a pore size of 75 ⁇ m, and an overall density of 0.13 g / cm 3 .
- the first papermaking material constituting the upper layer 80% of mercerized pulp as natural fibers and 20% of PET fibers having a fiber diameter of 12 ⁇ m as chemical fibers were used.
- the second papermaking raw material constituting the lower layer 20% of mercerized pulp and 65% of normal pulp without mercerization were blended as natural fibers, and 15% of PET fibers having a fiber diameter of 9 ⁇ m were blended as chemical fibers. A thing was used.
- a filter medium having a continuous density gradient was made by the wet papermaking method as shown in FIG.
- the supply amounts of the respective raw materials were adjusted so that the total basis weight was 100 g / m 2 and the basis weight ratio of the first papermaking raw material to the second papermaking raw material was 3: 7.
- the filter medium thus obtained had a thickness (thickness that was not calendered) of 0.60 mm, a pore size of 90 ⁇ m, and an overall density of 0.17 g / cm 3 .
- the first papermaking material constituting the upper layer 35% of mercerized pulp is used as natural fiber, 15% of normal pulp that is not mercerized, and PET having a fiber diameter of 18 ⁇ m as chemical fiber. A blend of 20% fiber and 30% PET fiber having a fiber diameter of 8 ⁇ m was used.
- the second papermaking material constituting the lower layer as natural fiber, 15% of mercerized pulp and 40% of normal pulp that is not mercerized, 35% of PET fiber having a fiber diameter of 8 ⁇ m as chemical fiber and fiber diameter Used was a 10% blend of 3 ⁇ m PET fiber.
- a filter medium having a continuous density gradient was made by the wet papermaking method as shown in FIG.
- the supply amounts of the respective raw materials were adjusted so that the overall basis weight was 80 g / m 2 and the basis weight ratio of the first papermaking raw material to the second papermaking raw material was 6: 4.
- the filter medium thus obtained had a thickness (thickness not calendared) of 0.56 mm, a pore size of 60 ⁇ m, and an overall density of 0.14 g / cm 3 .
- Comparative Examples 4 to 14 summarize the papermaking materials and physical property values of Comparative Examples 4 to 14.
- Comparative Examples 4, 5, and 6 have a two-layer structure using two low-density and high-density paper-making raw materials, and as in Examples 1 to 3, the paper-making method described in FIG. The paper was made to have a continuous density gradient.
- the remaining Comparative Examples 7 to 14 are single layers made of one type of papermaking raw material.
- FIG. 8 summarizes the results of testing the so-called dust performance of Examples 1 to 3 and Comparative Examples 4 to 14.
- air containing dust having a particle diameter of 7 ⁇ m defined as “fine dust” is continuously passed through a filter medium as a sample, and the amount of dust trapped until reaching a predetermined increase in ventilation resistance is measured.
- the shaft's dust holding capacity (DHC) is used, and the ratio of dust trapped to the amount of dust input is taken as the efficiency of the vertical axis.
- the overall performance (lifetime and trapping efficiency) of the filter media is expressed in one point. Is. In the figure, points # 1 to # 3 are Examples 1 to 3, and points # 4 to # 14 are Comparative Examples 4 to 14.
- FIG. 9 similarly summarizes the results of testing so-called carbon performance.
- This carbon performance test is the same as the carbon performance test described above except that carbon (soot) having a particle size of 0.5 ⁇ m is used instead of dust having a particle size of 7 ⁇ m.
- the horizontal axis represents carbon holding capacity (CHC).
- the filter medium of the present invention is not limited to an air cleaner, and can also be applied as a filter medium such as an oil filter or a fuel filter.
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Abstract
Description
上記第1の抄紙原料および上記第2の抄紙原料は、天然繊維と化学繊維とを含み、
上記第1の抄紙原料における化学繊維の配合比は上記第2の抄紙原料における化学繊維の配合比よりも高く、
上記第1の抄紙原料における化学繊維の太さが上記第2の抄紙原料における化学繊維の太さよりも太く、
坪量が60~250g/m2である。
天然繊維と化学繊維とを含む第1の抄紙原料と、天然繊維と化学繊維とを含む第2の抄紙原料と、を準備し、
ここで、上記第1の抄紙原料における化学繊維の配合比は上記第2の抄紙原料における化学繊維の配合比よりも高く、かつ、
上記第1の抄紙原料における化学繊維の太さが上記第2の抄紙原料における化学繊維の太さよりも太く、
これら2つの抄紙原料を用いて、坪量が60~250g/m2の範囲で、主に第1の抄紙原料からなる上層から主に第2の第2の抄紙原料からなる下層へと層間で両者の配合割合が連続的に変化するように抄紙を行う。
Claims (7)
- 上層用の第1の抄紙原料と下層用の第2の抄紙原料とを用いて、上層から下層へと層間で連続的な密度勾配を有するように抄紙したフィルタ用の濾材であって、
上記第1の抄紙原料および上記第2の抄紙原料は、天然繊維と化学繊維とを含み、
上記第1の抄紙原料における化学繊維の配合比は上記第2の抄紙原料における化学繊維の配合比よりも高く、
上記第1の抄紙原料における化学繊維の太さが上記第2の抄紙原料における化学繊維の太さよりも太く、
坪量が60~250g/m2である、フィルタ用の濾材。 - 上記第1の抄紙原料と上記第2の抄紙原料とが、坪量比で、2:8~6:4の割合で含まれてなる請求項1に記載のフィルタ用の濾材。
- 厚みが0.4~1.5mmの範囲にある請求項1または2に記載のフィルタ用の濾材。
- 密度が0.1~0.5g/cm3の範囲にある請求項1~3のいずれかに記載のフィルタ用の濾材。
- 上記第1の抄紙原料における化学繊維の配合比は、10~80%であり、その繊維の太さは、10~30μmであり、
上記第2の抄紙原料における化学繊維の配合比は、60%以下であり、その繊維の太さは、3~20μmである、請求項1~4のいずれかに記載のフィルタ用の濾材。 - 上記濾材は、抄紙後にプリーツ加工され、自動車用内燃機関のエアクリーナに用いられる、請求項1~5のいずれかに記載のフィルタ用の濾材。
- 天然繊維と化学繊維とを含む第1の抄紙原料と、天然繊維と化学繊維とを含む第2の抄紙原料と、を準備し、
ここで、上記第1の抄紙原料における化学繊維の配合比は上記第2の抄紙原料における化学繊維の配合比よりも高く、かつ、
上記第1の抄紙原料における化学繊維の太さが上記第2の抄紙原料における化学繊維の太さよりも太く、
これら2つの抄紙原料を用いて、坪量が60~250g/m2の範囲で、主に第1の抄紙原料からなる上層から主に第2の第2の抄紙原料からなる下層へと層間で両者の配合割合が連続的に変化するように抄紙を行う、フィルタ用の濾材の製造方法。
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CN201380032434.3A CN104470615B (zh) | 2012-06-21 | 2013-04-24 | 用于过滤器的过滤材料及其制造方法 |
KR1020147014921A KR101702730B1 (ko) | 2012-06-21 | 2013-04-24 | 에어 클리너용 여과재 및 그 제조 방법 |
US14/408,804 US20150211451A1 (en) | 2012-06-21 | 2013-04-24 | Filtering material for filter and production process therefor |
EP13806451.4A EP2865435B1 (en) | 2012-06-21 | 2013-04-24 | Filtering material for filter and production process therefor |
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JP2012139299A JP6030350B2 (ja) | 2012-06-21 | 2012-06-21 | エアクリーナ用の濾材の製造方法 |
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EP (1) | EP2865435B1 (ja) |
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KR101684152B1 (ko) | 2015-07-22 | 2016-12-07 | 도레이첨단소재 주식회사 | 필터 성능이 우수한 이형단면 폴리에스터 스테이플 섬유 여과제 및 그 제조방법 |
EP3380320B1 (en) * | 2015-11-27 | 2021-01-06 | Tetra Laval Holdings & Finance S.A. | Method of manufacturing a laminated packaging material, the packaging material obtained by the method and packaging containers manufactured therefrom |
JP2017196581A (ja) * | 2016-04-28 | 2017-11-02 | 株式会社マーレ フィルターシステムズ | フィルタ用の濾材の製造方法 |
US11117079B2 (en) * | 2017-01-20 | 2021-09-14 | Champion Laboratories, Inc. | Filter packs, processes for making filter packs, and air filters comprising filter packs |
DE102018004521A1 (de) * | 2018-06-07 | 2019-12-12 | Sartorius Stedim Biotech Gmbh | Serielle Anordnung mit mehreren Lagen asymmetrischer Filtermedien, Herstellungsverfahren, Filtrationseinheit, Verwendung der Anordnung und Charakterisierungsverfahren |
CN113509800B (zh) * | 2020-04-10 | 2022-09-30 | 中国科学技术大学 | 一种多尺度结构植物纤维空气过滤材料及其制备方法和用途 |
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- 2012-06-21 JP JP2012139299A patent/JP6030350B2/ja not_active Expired - Fee Related
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2013
- 2013-04-24 CN CN201380032434.3A patent/CN104470615B/zh not_active Expired - Fee Related
- 2013-04-24 EP EP13806451.4A patent/EP2865435B1/en not_active Not-in-force
- 2013-04-24 WO PCT/JP2013/062024 patent/WO2013190905A1/ja active Application Filing
- 2013-04-24 US US14/408,804 patent/US20150211451A1/en not_active Abandoned
- 2013-04-24 KR KR1020147014921A patent/KR101702730B1/ko active IP Right Grant
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JPS5317687A (en) | 1976-08-02 | 1978-02-17 | American Cyanamid Co | Polyquaternary polymer and process for producing same and agglomeration method |
JPH06240594A (ja) * | 1993-02-17 | 1994-08-30 | New Oji Paper Co Ltd | 掃除機フィルター用原紙 |
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KR20140085588A (ko) | 2014-07-07 |
EP2865435A1 (en) | 2015-04-29 |
JP2014000557A (ja) | 2014-01-09 |
US20150211451A1 (en) | 2015-07-30 |
KR101702730B1 (ko) | 2017-02-06 |
EP2865435B1 (en) | 2018-04-04 |
CN104470615B (zh) | 2016-08-31 |
JP6030350B2 (ja) | 2016-11-24 |
EP2865435A4 (en) | 2016-03-02 |
CN104470615A (zh) | 2015-03-25 |
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