WO2018221122A1 - フィルター用スパンボンド不織布およびその製造方法 - Google Patents
フィルター用スパンボンド不織布およびその製造方法 Download PDFInfo
- Publication number
- WO2018221122A1 WO2018221122A1 PCT/JP2018/017617 JP2018017617W WO2018221122A1 WO 2018221122 A1 WO2018221122 A1 WO 2018221122A1 JP 2018017617 W JP2018017617 W JP 2018017617W WO 2018221122 A1 WO2018221122 A1 WO 2018221122A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- polyester
- nonwoven fabric
- melting point
- dtex
- melting
- Prior art date
Links
Images
Classifications
-
- 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
- B01D39/1607—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
- B01D39/163—Other self-supporting filtering material ; Other filtering material of organic material, e.g. synthetic fibres the material being fibrous of synthetic origin sintered or bonded
-
- D—TEXTILES; PAPER
- D04—BRAIDING; LACE-MAKING; KNITTING; TRIMMINGS; NON-WOVEN FABRICS
- D04H—MAKING TEXTILE FABRICS, e.g. FROM FIBRES OR FILAMENTARY MATERIAL; FABRICS MADE BY SUCH PROCESSES OR APPARATUS, e.g. FELTS, NON-WOVEN FABRICS; COTTON-WOOL; WADDING ; NON-WOVEN FABRICS FROM STAPLE FIBRES, FILAMENTS OR YARNS, BONDED WITH AT LEAST ONE WEB-LIKE MATERIAL DURING THEIR CONSOLIDATION
- D04H3/00—Non-woven fabrics formed wholly or mainly of yarns or like filamentary material of substantial length
- D04H3/005—Synthetic yarns or filaments
- D04H3/009—Condensation or reaction polymers
- D04H3/011—Polyesters
-
- D—TEXTILES; PAPER
- D04—BRAIDING; LACE-MAKING; KNITTING; TRIMMINGS; NON-WOVEN FABRICS
- D04H—MAKING TEXTILE FABRICS, e.g. FROM FIBRES OR FILAMENTARY MATERIAL; FABRICS MADE BY SUCH PROCESSES OR APPARATUS, e.g. FELTS, NON-WOVEN FABRICS; COTTON-WOOL; WADDING ; NON-WOVEN FABRICS FROM STAPLE FIBRES, FILAMENTS OR YARNS, BONDED WITH AT LEAST ONE WEB-LIKE MATERIAL DURING THEIR CONSOLIDATION
- D04H3/00—Non-woven fabrics formed wholly or mainly of yarns or like filamentary material of substantial length
- D04H3/08—Non-woven fabrics formed wholly or mainly of yarns or like filamentary material of substantial length characterised by the method of strengthening or consolidating
- D04H3/14—Non-woven fabrics formed wholly or mainly of yarns or like filamentary material of substantial length characterised by the method of strengthening or consolidating with bonds between thermoplastic yarns or filaments produced by welding
- D04H3/147—Composite yarns or filaments
-
- 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
- B01D2239/02—Types of fibres, filaments or particles, self-supporting or supported materials
- B01D2239/0216—Bicomponent or multicomponent fibres
-
- 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
- B01D2239/02—Types of fibres, filaments or particles, self-supporting or supported materials
- B01D2239/0216—Bicomponent or multicomponent fibres
- B01D2239/0233—Island-in-sea
-
- 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
- B01D2239/0618—Non-woven
-
- 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
- B01D2239/0627—Spun-bonded
-
- 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
- B01D2239/0668—The layers being joined by heat or melt-bonding
-
- 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
- B01D2239/10—Filtering material manufacturing
-
- 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
-
- 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
- B01D2239/125—Size distribution
-
- 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
- B01D2239/1291—Other parameters
-
- D—TEXTILES; PAPER
- D10—INDEXING SCHEME ASSOCIATED WITH SUBLASSES OF SECTION D, RELATING TO TEXTILES
- D10B—INDEXING SCHEME ASSOCIATED WITH SUBLASSES OF SECTION D, RELATING TO TEXTILES
- D10B2331/00—Fibres made from polymers obtained otherwise than by reactions only involving carbon-to-carbon unsaturated bonds, e.g. polycondensation products
- D10B2331/04—Fibres made from polymers obtained otherwise than by reactions only involving carbon-to-carbon unsaturated bonds, e.g. polycondensation products polyesters, e.g. polyethylene terephthalate [PET]
-
- D—TEXTILES; PAPER
- D10—INDEXING SCHEME ASSOCIATED WITH SUBLASSES OF SECTION D, RELATING TO TEXTILES
- D10B—INDEXING SCHEME ASSOCIATED WITH SUBLASSES OF SECTION D, RELATING TO TEXTILES
- D10B2505/00—Industrial
- D10B2505/04—Filters
Definitions
- the present invention relates to a spunbond nonwoven fabric for a filter used for a pleated filter substrate to be bonded to a pleated filter or a filter medium such as a polytetrafluoroethylene (PTFE) film or nanofiber, and a method for producing the same.
- PTFE polytetrafluoroethylene
- nonwoven fabrics used as pleated filters include high rigidity for pleating, air permeability for low pressure loss, and fineness that improves dust removal by filtering dust on the surface layer.
- various woven and non-woven fabrics have been proposed.
- Patent Document 5 Japanese Patent No. 3534043 JP 7-157960 A JP 2009-6318 A Japanese Patent Laid-Open No. 11-192406 JP-A-11-90135
- Patent Document 2 if it is an air-through method, there is no thermal bonding part such as an embossing roll, and there is no problem of impairing the air permeability. Backwashing has a problem in that dust cannot be removed and the life is shortened.
- Patent Document 4 since the mesh is composed of filaments of 1 denier (1.111 dtex) or less, although high collection performance can be obtained, there is a problem that air permeability is lost, high pressure loss occurs and life is shortened. there were.
- Patent Document 5 is not preferable as a pleated filter because the fibers constituting the nonwoven fabric have poor strength, low air permeability, and high pressure loss.
- an object of the present invention is to provide a spunbond nonwoven fabric for a filter that has high rigidity and air permeability in a large fineness layer and is also excellent in dust removal properties in a fineness fineness layer. is there.
- Another object of the present invention is to provide a production method for efficiently and stably producing a spunbond nonwoven fabric for a filter having the above performance.
- the spunbond nonwoven fabric for filters of the present invention has the following configuration. That is, A spunbond nonwoven fabric comprising a composite polyester fiber in which a low melting point polyester having a melting point lower by 10 to 140 ° C. than the melting point of the high melting point polyester is disposed around the high melting point polyester, And the single layer fineness of the composite polyester fiber of the surface layer portion is 1 dtex or more and less than 3 dtex, the single fiber fineness of the back layer portion is 3 dtex or more and 5 dtex or less, and the basis weight of the spunbonded nonwoven fabric is 130 A spunbond nonwoven fabric for filters, which is ⁇ 300 g / m 2 .
- the manufacturing method of the spun bond nonwoven fabric for filters of this invention has the following structure. That is, A method for producing a spunbonded nonwoven fabric for filters, wherein the following steps (a) to (d) are sequentially performed. (A) A step of spinning a composite polyester fiber in which a low-melting polyester having a melting point lower by 10 to 140 ° C. than the melting point of the high-melting polyester is arranged around the high-melting polyester from the spinneret.
- the spun composite polyester fiber is sucked and stretched with a high-speed suction gas, collected on a moving net conveyor, and a surface layer portion having a single fiber fineness of 1 dtex or more and less than 3 dtex and a single fiber fineness of 3 dtex or more and 5 dtex or less.
- the process of obtaining the fiber web which consists of a composite type polyester fiber of the back layer part.
- C A step of allowing hot air having a temperature higher than the melting point of the low-melting polyester and lower than the melting point of the high-melting polyester to pass through the obtained fiber web and performing air-through heat bonding.
- the composite form of the composite polyester fiber is a core-sheath type in which the high-melting polyester is a core component and the low-melting polyester is a sheath component. And the core-sheath component mass ratio of the core component to the sheath component is 90:10 to 60:40.
- spunbond nonwoven fabric for filters of the present invention there is no partial recess having a depth of 0.1 mm or more on at least one surface of the spunbond nonwoven fabric for filters.
- the high melting point polyester is polyethylene terephthalate
- the low melting point polyester is copolymer polyethylene terephthalate
- the composite form of the composite polyester fiber is a core sheath having the high melting point polyester as a core component and the low melting point polyester as a sheath component.
- the mass ratio of the core-sheath component to the core component is 90:10 to 60:40.
- the high melting point polyester is polyethylene terephthalate
- the low melting point polyester is copolymer polyethylene terephthalate
- the spunbond nonwoven fabric for filters of the present invention can be suitably used as a pleated filter substrate to be bonded to a filter medium such as a pleated filter, a PTFE membrane, or nanofiber.
- a spunbond nonwoven fabric for a filter of the present invention a spunbond nonwoven fabric for a filter having the above performance can be produced efficiently and stably.
- the spunbond nonwoven fabric for a filter of the present invention is a spunbond nonwoven fabric composed of a composite type polyester fiber in which a low melting point polyester having a melting point lower by 10 to 140 ° C. than the melting point of the high melting point polyester is arranged around the high melting point polyester.
- the spunbond nonwoven fabric has a surface layer portion and a back layer portion, the single fiber fineness of the composite polyester fiber of the surface layer portion is 1 dtex or more and less than 3 dtex, and the single fiber fineness of the back layer portion is 3 dtex or more and 5 dtex or less.
- the basis weight of the spunbonded nonwoven fabric is 130 to 300 g / m 2 .
- the surface layer portion is the dust collecting surface side when using the spunbond nonwoven fabric for filters as a filter
- the back layer portion refers to the surface opposite to the surface layer portion
- the spunbond nonwoven fabric for a filter of the present invention has an apparent density of 0.25 to 0.40 g / cm 3 and an air permeability per unit weight of 0.05 to 0.50 (cm 3 / cm 2 ⁇ sec) / ( g / m 2 ) and at least one of the vertical direction and the horizontal direction is preferably 0.08 to 0.32 (mN) / (g / m 2 ).
- Polyester is used as a raw material resin for the synthetic fibers constituting the spunbond nonwoven fabric for filters of the present invention.
- Polyester is a high molecular polymer having an acid component and an alcohol component as monomers.
- the acid component include aromatic carboxylic acids such as terephthalic acid, isophthalic acid and phthalic acid, aliphatic dicarboxylic acids such as adipic acid and sebacic acid, and alicyclic dicarboxylic acids such as cyclohexanecarboxylic acid.
- the alcohol component ethylene glycol, diethylene glycol, polyethylene glycol, or the like can be used.
- polyesters examples include polyethylene terephthalate (PET), polybutylene terephthalate (PBT), polytrimethylene terephthalate (PTT), polyethylene naphthalate, polylactic acid, and polybutylene succinate. Most preferably used is PET, which has a high melting point, excellent heat resistance, and excellent rigidity.
- Examples of the combination of the high-melting polyester and the low-melting polyester (high-melting polyester / low-melting polyester) used in the present invention include PET / PBT, PET / PTT, PET / polylactic acid, and PET / copolymerized PET.
- PET / PBT PET / PTT
- PET / polylactic acid PET / copolymerized PET
- a combination of PET / copolymerized PET is preferably used because of excellent spinnability.
- isophthalic acid copolymerized PET is preferably used because it is particularly excellent in spinnability.
- a crystal nucleating agent, a matting agent, a pigment, an antifungal agent, an antibacterial agent, a flame retardant, a hydrophilic agent, and the like can be added to the polyester raw material as long as the effects of the present invention are not impaired.
- metal oxides such as titanium oxide improve the spinnability by reducing the surface friction of the fibers and preventing the fusion between the fibers, and increase the thermal conductivity during thermocompression molding with a non-woven hot roll. This has the effect of improving the adhesion of the nonwoven fabric.
- aliphatic bisamides such as ethylene bis-stearic acid amide and / or alkyl-substituted aliphatic monoamides have the effect of enhancing the releasability between the hot roll and the nonwoven web and improving the transportability.
- the polyester fiber constituting the spunbond nonwoven fabric for a filter of the present invention is a composite polyester fiber in which a low-melting polyester having a melting point 10 to 140 ° C. lower than the melting point of the high-melting polyester is arranged around the high-melting polyester. It is.
- a low-melting polyester having a melting point lower by 10 to 140 ° C. than the melting point of the high-melting polyester is arranged around the high-melting polyester, the spunbond nonwoven is formed when the spunbond nonwoven is formed and used by thermal bonding. Since the composite polyester fibers (filaments) to be bonded firmly to each other, the spunbond nonwoven fabric for filters is excellent in mechanical strength and can sufficiently withstand repeated backwashing.
- the melting point of the low melting point polyester in the present invention is not lower than the melting point of the high melting point polyester by 10 ° C. or more, the desired thermal adhesiveness cannot be obtained. The decline cannot be suppressed.
- a more preferable range of the melting point difference between the high melting point polyester and the low melting point polyester used in the present invention is 20 to 120 ° C., and a further preferable range is 30 to 100 ° C.
- the melting point of the high melting point polyester is preferably in the range of 200 to 320 ° C.
- the melting point of the high melting point polyester is preferably 200 ° C. or higher, more preferably 210 ° C. or higher, and further preferably 220 ° C. or higher.
- the melting point of the high-melting polyester is preferably 320 ° C. or lower, more preferably 300 ° C. or lower, and further preferably 280 ° C. or lower. Can be suppressed.
- the melting point of the low melting point polyester is preferably in the range of 160 to 250 ° C.
- the melting point of the low-melting polyester is preferably 160 ° C. or higher, more preferably 170 ° C. or higher, and even more preferably 180 ° C. or higher. Is also excellent in form stability.
- the melting point of the low-melting polyester is preferably 250 ° C. or lower, more preferably 240 ° C. or lower, a filter having excellent thermal adhesiveness and excellent mechanical strength during the production of the nonwoven fabric can be obtained.
- the content ratio of the high-melting polyester and the low-melting polyester is preferably in the range of 90:10 to 60:40, and more preferably in the range of 85:15 to 70:30.
- the rigidity and heat resistance of the spunbonded nonwoven fabric can be improved.
- the low melting point polyester to 10 to 40% by mass, the composite polyester fibers (filaments) constituting the spunbond nonwoven fabric can be firmly bonded to each other when the spunbond nonwoven fabric is formed and used by thermal bonding. Excellent strength and can withstand repeated backwashing.
- the composite form of the composite polyester fiber includes, for example, a concentric core-sheath type, an eccentric core-sheath type, and a sea-island type.
- the filaments can be bonded uniformly and firmly, so that the composite form is concentric.
- a core-sheath type is preferable.
- examples of the cross-sectional shape of the filament (single fiber) include circular cross-sections, flat cross-sections, polygonal cross-sections, multi-leaf cross-sections, and hollow cross-sections.
- the spunbond nonwoven fabric for a filter according to the present invention preferably has no partial concave portion having a depth of 0.1 mm or more on at least one surface, and no partial concave portion having a depth of 0.1 mm or more on both surfaces.
- a partial recessed part is produced when fibers are densely filled in the thickness direction by an embossing roll or partial thermocompression bonding by ultrasonic bonding.
- a partial recess having a depth of 0.1 mm or more means that when the surface of a spunbond nonwoven fabric is viewed from the vertical direction, a single yarn jumps out of the surface shape measured on a straight line having a length of 3 to 10 mm with fuzz etc.
- the highest part is the reference point (depth 0 mm), and there is a continuous concave part having a depth of 0.1 mm or more in the thickness direction, 0.2 mm or more in the surface direction. Point to the point.
- This partial recess is measured by measuring the surface shape using a non-contact type shape measuring instrument such as a shape analysis laser microscope or a 3D shape measuring machine, or by using a scanning electron microscope to measure the cross-sectional thickness of the spunbond nonwoven fabric. It can measure by measuring. Due to the absence of such a partial recess, the dust removal performance can be improved and a longer-life filter can be obtained.
- a non-contact type shape measuring instrument such as a shape analysis laser microscope or a 3D shape measuring machine
- a spunbond nonwoven fabric having no partial recesses is a fiber web composed of a composite polyester fiber in which a low-melting polyester having a melting point 10 to 140 ° C. lower than the melting point of the high-melting polyester is arranged around the high-melting polyester. After passing hot air at a temperature higher than the melting point of the low-melting polyester and lower than the melting point of the high-melting polyester, air-through heat-bonded, and sandwiched between a pair of flat rolls or two belt conveyors, It can be obtained by heat treatment at a temperature 5 to 75 ° C. lower than the melting point.
- the single fiber fineness of the composite polyester fiber in the surface layer part constituting the spunbond nonwoven fabric for filter is in the range of 1 dtex or more and less than 3 dtex, and the single fiber fineness of the back layer part is in the range of 3 dtex or more and 5 dtex or less.
- the monofilament fineness of the composite polyester fiber in the surface layer is less than 1 dtex, the pressure loss tends to increase with a decrease in the air permeability of the spunbonded nonwoven fabric, and the production stability is inferior because yarn breakage is likely to occur during production. .
- the single fiber fineness of the composite polyester fiber in the surface layer portion is 3 dtex or more, there is a problem that dust tends to enter the inside because it is inferior in denseness.
- the single fiber fineness of the composite polyester fiber in the back layer portion is less than 3 dtex, the pressure loss tends to be high, and the dust removal property is inferior and the life is shortened.
- the single fiber fineness of the composite polyester fiber in the back layer exceeds 5 dtex, the collection performance tends to decrease with the uniformity of the spunbonded nonwoven fabric, and yarn breakage occurs due to poor cooling of the filament during production. It is inferior in production stability.
- the more preferable range of the single fiber fineness of the surface layer portion of the composite type polyester fiber is a range of 1.2 dtex or more and 2.9 dtex or less.
- the range of the single fiber fineness of a more preferable back layer part is the range of 3.0 dtex or more and 4.5 dtex or less.
- the single fiber fineness refers to the value obtained as follows. That is, 10 small sample samples were randomly collected from the spunbonded nonwoven fabric, photographed at 500 to 3000 times with a scanning electron microscope or the like, 10 fibers from each sample, 100 fibers in total were arbitrarily selected, Measure its thickness. The fiber is assumed to have a circular cross section, and the thickness is the fiber diameter. The fineness is calculated from the fiber diameter calculated by rounding off the first decimal place of the average value and the density of the polymer, and the first decimal place is rounded off.
- the basis weight of the spunbond nonwoven fabric for filters in the present invention is in the range of 130 to 300 g / m 2 . If the basis weight is less than 130 g / m 2 , the rigidity required for the pleats cannot be obtained. On the other hand, when the basis weight exceeds 300 g / m 2 , it is not possible to suppress an increase in pressure loss, and further, the cost is inferior.
- a more preferable range of the basis weight is 130 to 260 g / m 2 , and further preferably 150 to 240 g / m 2 .
- the basis weight here means that three samples with a size of 50 cm in length and 50 cm in width are collected and each mass is measured, and the average value of the obtained values is converted per unit area, and the first decimal place is given. Calculated by rounding off.
- the thickness of the spunbond nonwoven fabric for filters in the present invention is preferably 0.35 to 1.2 mm, more preferably 0.38 to 1.0 mm, and still more preferably 0.40 to 0.8 mm.
- the rigidity can be improved and a nonwoven fabric suitable for use as a filter can be obtained.
- it can be set as the nonwoven fabric excellent in the handleability and workability as a filter by making thickness into 1.2 mm or less.
- the apparent density of the spunbond nonwoven fabric for filters in the present invention is preferably 0.25 to 0.40 g / cm 3 .
- the apparent density is 0.25 to 0.40 g / cm 3
- the spunbonded nonwoven fabric has a dense structure, and dust is difficult to enter inside, and is excellent in dust removal properties.
- a more preferable range of the apparent density is 0.27 to 0.40 g / cm 3
- a further preferable range is 0.30 to 0.40 g / cm 3 .
- the apparent density is calculated by the following equation.
- the air permeability per unit weight of the spunbond nonwoven fabric for filters is preferably 0.05 to 0.50 ((cm 3 / cm 2 ⁇ sec) / (g / m 2 )). It is possible to suppress an increase in pressure loss when the air flow per basis weight is 0.05 ((cm 3 / cm 2 ⁇ sec) / (g / m 2 )) or more.
- the air flow rate per unit weight is 0.50 ((cm 3 / cm 2 ⁇ sec) / (g / m 2 )) or less, the dust is less likely to stay inside, so that the dust removal property is good. is there.
- a more preferable air flow rate per unit weight is 0.10 to 0.48 ((cm 3 / cm 2 ⁇ sec) / (g / m 2 )), and a more preferable air flow rate per unit weight is 0.15 to 0.00. 45 ((cm 3 / cm 2 ⁇ sec) / (g / m 2 )).
- the air flow per unit weight is calculated by the following formula.
- the bending resistance per unit weight of the spunbond nonwoven fabric for filters in the present invention is 0.08 to 0.32 ((mN) / (g / m 2 )) in at least one of the vertical direction and the horizontal direction. It is preferable.
- the bending resistance per basis weight is 0.08 ((mN) / (g / m 2 )) or more, the pleating property is excellent, and the spunbond nonwoven fabric for filters is difficult to be deformed during backwashing.
- the bending resistance per basis weight is 0.32 (mN) / (g / m 2 ) or less, the folds are hardly formed when the spunbond nonwoven fabric for a filter is wound up, resulting in high quality.
- the bending resistance per unit weight is calculated by the following equation.
- Bending softness per unit weight ((mN) / (g / m 2 )) Bending softness (mN) / Weight per unit (g / m 2 )
- the vertical direction refers to the sheet conveying direction during the production of the spunbonded nonwoven fabric, that is, the winding direction in the nonwoven fabric roll
- the horizontal direction refers to the direction orthogonal to the sheet conveying direction during the production of the spunbonded nonwoven fabric, that is, The width direction in a nonwoven fabric roll is pointed out.
- the softness per unit area of the spunbonded nonwoven fabric of the present invention is 0.08 to 0.32 ((mN) / (g / m 2 )) in at least one of the vertical direction and the horizontal direction.
- the tensile strength in the vertical direction per unit weight of the spunbond nonwoven fabric for filters of the present invention (hereinafter, sometimes referred to as the vertical tensile strength per unit weight) is 3.2 (N / 5 cm) / (g / m 2). ) Or more, more preferably 3.5 (N / 5 cm) / (g / m 2 ) or more, and still more preferably 3.8 (N / 5 cm) / (g / m 2 ) or more. is there.
- the horizontal tensile strength per unit weight (hereinafter, sometimes referred to as horizontal tensile strength per unit weight) is preferably 2.0 (N / 5 cm) / (g / m 2 ) or more. More preferably, it is 2.3 (N / 5 cm) / (g / m 2 ) or more, and further preferably 2.5 (N / 5 cm) / (g / m 2 ) or more.
- the tensile strength per unit weight is calculated by the following equation.
- the spunbond nonwoven fabric for a filter of the present invention has a specific basis weight, front and back single fiber fineness, apparent density, air flow rate, and bending resistance, thereby reducing low-pressure loss and dust.
- a spunbond nonwoven fabric for a filter that is excellent in the wiping off property and is suitable and useful as a long-life filter that cannot be achieved by the prior art can be obtained.
- the spunbond nonwoven fabric for filters of the present invention is produced by sequentially performing the following steps (a) to (d).
- (A) A step of spinning a composite polyester fiber in which a low-melting polyester having a melting point lower by 10 to 140 ° C. than the melting point of the high-melting polyester is arranged around the high-melting polyester from the spinneret.
- (B) The spun composite polyester fiber is sucked and stretched with a high-speed suction gas, collected on a moving net conveyor, and a surface layer portion having a single fiber fineness of 1 dtex or more and less than 3 dtex and a single fiber fineness of 3 dtex or more and 5 dtex or less.
- the process of obtaining the fiber web which consists of a composite type polyester fiber of the back layer part.
- C A step of allowing hot air having a temperature higher than the melting point of the low-melting polyester and lower than the melting point of the high-melting polyester to pass through the obtained fiber web and performing air-through heat bonding.
- D The air-through thermally bonded fiber web is sandwiched between a pair of flat rolls or two belt conveyors, and heat treated at a temperature 5 to 75 ° C. lower than the melting point of the low-melting polyester.
- the spunbond nonwoven fabric for a filter of the present invention is obtained by a so-called spunbond method.
- a fiber web collected by the spunbond method is melted with low-melting polyester by an air-through method, and the fibers are bonded to each other.
- a method of performing heat treatment is applied.
- thermocompression bonding temperature for temporary bonding is preferably 70 to 120 ° C. lower than the melting point of the low-melting polyester.
- a fiber web having a single fiber fineness of 3 dtex or more and 5 dtex or less after collecting the fiber web having a single fiber fineness of 1 dtex or more and less than 3 dtex on a net conveyor.
- a fiber web having a single fiber fineness of 3 dtex or more and 5 dtex or less may be collected on a net conveyor, and a fiber web having a single fiber fineness of 1 dtex or more and less than 3 dtex may be collected and laminated.
- a sheet obtained by temporarily adhering a fiber web having a single fiber fineness of 1 dtex or more and less than 3 dtex and a sheet obtained by temporarily adhering a fiber web having a single fiber fineness of 3 dtex or more and 5 dtex or less can be obtained by laminating.
- the air-through method in the present invention is a method in which hot air is passed through the fiber web obtained by the spunbond method, and the temperature of the hot air is higher than the melting point of the low-melting polyester and lower than the melting point of the high-melting polyester. This is very important.
- the range of the hot air temperature is preferably the melting point of the low melting point polyester + 5 ° C. to the melting point of the high melting point polyester ⁇ 5 ° C.
- the hot air temperature is lower than that of the low-melting polyester, it is difficult to fuse the fibers together and the mechanical strength is poor.
- the hot air temperature is higher than that of the high-melting polyester, all the fibers constituting the spunbonded nonwoven fabric are melted, resulting in a film-like sheet, poor air permeability, and difficult to use as a pleated filter.
- the fiber web obtained by the air-through method has a bulky and low-density structure, and when used as a pleated filter, it has high air permeability, dust can enter inside, and it cannot be wiped off with compressed air, resulting in a low life.
- the present invention in particular, by densifying the surface of the fiber sheet, it is possible to perform filtration on the surface layer of the fiber web while maintaining air permeability, which is a feature of the air-through method. It is to improve.
- the air-through thermal bonding of the present invention is preferably performed in a state where the fiber web is gripped over the entire surface.
- the method of gripping the entire surface of the fiber web is to pass between a pair of upper and lower conveyor nets and to bring the conveyor net into contact with both sides of the fiber web, or to contact the air-through drum under tension, and the frictional force with the drum
- a gripping method is preferably used.
- a densification method a method of densifying the fibers on the surface of the fiber web by heat bonding using a pair of flat rolls, or heat treatment by sandwiching a fiber sheet between two belt conveyors made of resin belts The method of doing is mentioned.
- the method of heat-treating the fiber web between the belt conveyors can heat-treat over a relatively long time without positively applying pressure, so that only the surface of the fiber web can be densified, This is the preferred method.
- the temperature when heat-treating with a pair of flat rolls or two belt conveyors is 5 to 75 ° C. lower than the melting point of the low melting point polyester existing on the fiber surface of the spunbond nonwoven fabric.
- a lower temperature is preferable, and a lower temperature of 20 to 60 ° C. is a more preferable embodiment.
- the heat treatment temperature by a pair of flat rolls or two belt conveyors is not lower than the melting point of the low melting point polyester existing on the fiber surface of the spunbonded nonwoven fabric by 5 ° C. or more, it becomes excessive thermal bonding, and is specified in the present invention. It becomes smaller than the lower limit of the density range.
- the thermal adhesion becomes weak and the surface is densified. It becomes insufficient and becomes larger than the upper limit of the specific density range defined in the present invention.
- the spunbond nonwoven fabric for a filter of the present invention preferably has an operating time of 1,000 to 5,000 hours, more preferably 1,500 to 4,000 hours, more preferably 2,000 to 4,000 hours in the dust removal test. More preferred is 3,500 hours.
- the dust wiping-out test is measured by the following method or a measurement method that can obtain the equivalent result. That is, three samples of 15 cm ⁇ 15 cm are taken from an arbitrary portion of the nonwoven fabric, and each test apparatus has a dust supply device 5 on the upstream side of the sample holder 1 for setting the test sample M as shown in FIG.
- the flowmeter 2, the flow rate adjustment valve 3, the blower 4, and the pulse jet device 6 are connected to the downstream side. Evaluation area of the test sample was 0.01 m 2.
- a pressure gauge 7 is connected to the sample holder 1 so that the pressure loss of the test sample M can be measured.
- the JIS15 standard powder is supplied from the dust supply device 5 so as to have a concentration of 20 g / m 3 , and the flow rate adjusting valve 3 so that the filter passing speed becomes 1.5 m / min.
- the air volume is adjusted with, the dust is continuously supplied at a constant concentration, and when the pressure loss of the test sample M reaches 1,500 Pa, 0.5 MPa compressed air is injected from the pulse jet device 6 for 0.1 sec.
- the dust adhering to the test sample M was removed.
- the operation time (hr) until the number of payouts reaches 200 times is measured, the average value of the test results of three times is obtained, and the first place is rounded to the operation time (hr). .
- ⁇ is the viscosity of the polymer solution
- ⁇ 0 is the viscosity of the orthochlorophenol
- t is the drop time of the solution (seconds)
- d is the density of the solution (g / cm 3 )
- t 0 is the drop of the orthochlorophenol.
- time (second) d 0 represents the density (g / cm 3 ) of orthochlorophenol, respectively)
- the intrinsic viscosity IV was calculated from the relative viscosity ⁇ r by the following formula.
- Non-woven fabric thickness (mm) Using a thickness gauge (“TECLOCK” (registered trademark) SM-114 manufactured by Teclock Co., Ltd.), measure the thickness of the nonwoven fabric at equal intervals in the width direction and round off the third decimal place from the average value. It was.
- TECLOCK registered trademark
- Apparent density weight per unit area (g / m 2 ) / thickness (mm) / 1,000 (7)
- Aeration rate of non-woven fabric (cm 3 / cm 2 ⁇ sec) Ten samples of 10 cm ⁇ 10 cm were taken from an arbitrary part of the spunbonded nonwoven fabric and measured by the fragile method based on JIS L 1913 (2010 edition). The set pressure during measurement was 125 Pa. The ventilation rate is calculated by rounding off the average value of the obtained 10 ventilation rates to the first decimal place.
- Aeration rate per unit weight of nonwoven fabric ((cm 3 / cm 2 ⁇ sec) / (g / m 2 )) Divide the air flow value obtained with the air flow rate in (7) above by the basis weight value obtained in the above (4) basis weight, and calculate the air flow rate per basis weight by rounding off to the fourth decimal place. To do.
- Non-woven bending resistance (9)
- the bending resistance is measured and determined according to the Gurley method described in JIS L 1913 (2010 edition) 6.7.4.
- Tensile strength of nonwoven fabric (N / 5cm)
- the tensile strength of the non-woven fabric is 5 cm ⁇ 30 cm test pieces each having a long side in the vertical direction and the horizontal direction in accordance with JIS L 1913 (2010 edition) 6.3.1. A point was collected, and a tensile test was performed using a constant-speed extension type tensile tester under the conditions of a grip interval of 20 cm and a tensile speed of 10 cm / min.
- the tensile strength (N / 5 cm) was determined by reading the strength at break and rounding off the first decimal place.
- the JIS15 standard powder is supplied from the dust supply device 5 so as to have a concentration of 20 g / m 3 , and the flow rate adjusting valve 3 so that the filter passing speed becomes 1.5 m / min.
- the air volume is adjusted with, the dust is continuously supplied at a constant concentration, and when the pressure loss of the test sample M reaches 1,500 Pa, 0.5 MPa compressed air is injected from the pulse jet device 6 for 0.1 sec. The dust adhering to the test sample M was removed.
- the operation time (hr) until the number of payouts reached 200 times was measured, the average value of the three test results was obtained, and the operation time (hr) was obtained by rounding off the first place.
- an aging cycle in which 0.5 MPa of compressed air was injected for 1 second every 5 seconds from a pulse jet device was performed 5,000 times. Subsequently, as a performance evaluation after aging, after the pressure loss reaches 1,000 Pa, a discharge cycle in which compressed air of 0.5 MPa is injected for 1 second (however, the pressure loss is less than 5 seconds from the previous discharge) When the pressure reaches 1,000 Pa, the compressed air is injected after dust loading until 5 seconds later.) Is repeated 30 times, and the dust collection rate is calculated based on the following formula from the powder leakage concentration during the test. The average of the measurements was taken and rounded to the fourth decimal place.
- Dust collection rate (%) (1-powder leakage concentration (g / m 3 ) / upstream dust concentration (g / m 3 )) ⁇ 100
- the pressure loss after 5 seconds from the ejection of the pulse jet in the thirty-th removal cycle was measured, the average of the three measurements was taken, and the first decimal place was rounded off.
- the highest point in the plane is defined as a reference point (depth 0 mm), and a straight line having a width direction of 4.5 mm and a longitudinal direction of 4.5 mm passing through the reference point Further, the presence or absence of a portion where the portion having a depth of 0.1 mm or more continues in the plane direction by 0.2 mm or more (that is, a partial recess having a depth of 0.1 mm or more) was investigated.
- Table 1 describes “None” when there is no partial recess having such a depth of 0.1 mm or more in any of the small sample, and the depth is zero in at least one small sample only on one side.
- Example 1 Polyethylene terephthalate (PET) having an intrinsic viscosity IV of 0.65 and a melting point of 260 ° C., dried to a moisture content of 50 mass ppm or less, and an intrinsic viscosity IV of 0.64, dried to a moisture content of 50 mass ppm or less, Copolymer polyester (CO-PET) having a polymerization rate of 11 mol% and a melting point of 230 ° C. was melted at temperatures of 295 ° C. and 280 ° C., respectively, using polyethylene terephthalate as a core component and copolymer polyester as a sheath component.
- PET Polyethylene terephthalate
- CO-PET Copolymer polyester
- a fiber web having a single fiber fineness of 2.1 dtex was collected and a single fiber fineness of 3.4 dtex (dt). Fibers were collected web of x). After passing air having a hot air temperature of 250 ° C. through the collected fiber web, it is thermally bonded by a calender roll comprising a pair of flat rolls at a temperature of 180 ° C. and a linear pressure of 50 kg / cm.
- a spunbonded nonwoven fabric having a basis weight of 200 g / m 2 and a fiber having a single fiber fineness of 2.1 dtex and a single fiber fineness of 3.4 dtex was obtained.
- the vertical tensile strength per unit weight of the obtained spunbonded nonwoven fabric is 4.3 (N / 5 cm) / (g / m 2 ), and the horizontal tensile strength per unit weight is 3.0 (N / 5 cm) / (g / M 2 ).
- Table 1 The results are shown in Table 1.
- Example 2 The single fiber fineness of the surface layer portion is 2.1 decitex (dtex) single fiber in the same condition as Example 1 except that the speed of the net conveyor is adjusted and the basis weight is changed to 260 g / m 2.
- a spunbonded nonwoven fabric having a basis weight of 260 g / m 2 was obtained, which was made of fibers having a fineness of 3.4 dtex. The results are shown in Table 1.
- Example 3 Polyethylene terephthalate (PET) having an intrinsic viscosity IV of 0.65 and a melting point of 260 ° C. dried to a water content of 50 mass ppm or less, and an intrinsic viscosity IV of 0.64 and an isophthalic acid copolymer dried to a water content of 50 mass ppm or less
- a copolymer polyester (CO-PET) having a rate of 11 mol% and a melting point of 230 ° C. is melted at temperatures of 295 ° C. and 280 ° C., respectively, using polyethylene terephthalate as a core component and copolymer polyester as a sheath component.
- a spunbonded nonwoven fabric having a basis weight of 200 g / m 2 and a fiber having a fiber fineness of 2.1 dtex and a single fiber fineness of 3.4 dtex was obtained.
- the vertical tensile strength per unit weight of the obtained spunbonded nonwoven fabric is 4.0 (N / 5 cm) / (g / m 2 ), and the horizontal tensile strength per unit weight is 2.7 (N / 5 cm) / (g / M 2 ).
- Table 1 The results are shown in Table 1.
- Example 4 The single fiber fineness of the surface layer portion is 2.1 decitex (dtex) under the same conditions as in Example 3 except that the basis weight is changed to 150 g / m 2 by adjusting the speed of the net conveyor. A spunbonded nonwoven fabric having a basis weight of 150 g / m 2 was obtained, which consisted of 3.4 dtex fiber. The results are shown in Table 1.
- Example 5 A fiber web having a single fiber fineness of 1.5 dtex was collected on the moving net conveyor under the same conditions as in Example 3 except that the single yarn fiber fineness was changed by adjusting the discharge amount.
- a fiber web having a single fiber fineness of 4.0 decitex (dtex) is collected thereon, and a single fiber fineness of the surface layer portion is 1.5 decitex (dtex), and a single fiber fineness of the back layer portion is 4.0 decitex (dtex).
- the spunbonded nonwoven fabric having a basis weight of 200 g / m 2 was obtained. The results are shown in Table 1.
- the properties of the obtained nonwoven fabric are as shown in Table 1.
- the spunbond nonwoven fabrics of Examples 1, 2, 3, 4 and 35 are all excellent in air permeability and rigidity, and after the dust removal test. These filters had dust on the surface, but they were not clogged and were all good. The results are shown in Table 1.
- Example 1 A spunbonded nonwoven fabric having a basis weight of 200 g / m 2 was obtained under the same conditions as in Example 1 except that the single fiber fineness was 2.7 dtex.
- the vertical tensile strength per unit weight of the obtained spunbonded nonwoven fabric is 4.4 (N / 5 cm) / (g / m 2 ), and the horizontal tensile strength per unit weight is 3.1 (N / 5 cm) / (g / M 2 ).
- Table 2 The results are shown in Table 2.
- Example 3 After passing air at a hot air temperature of 250 ° C. through a fiber sheet, it was sandwiched between two belt conveyors made of resin belts and heat-treated at a temperature of 170 ° C., under the same conditions as in Example 1. A spunbonded nonwoven fabric having a basis weight of 200 g / m 2 and having a single fiber fineness of 2.7 dtex was obtained. The results are shown in Table 2.
- PET Polyethylene terephthalate
- CO-PET Copolymer polyester
- Example 8 A fiber web having a single fiber fineness of 0.8 dtex was collected on a moving net conveyor under the same conditions as in Example 3 except that the single fiber fineness was changed by adjusting the discharge amount. A fiber web having a single fiber fineness of 4.5 dtex is collected, and a single fiber fineness of the surface layer portion is 1.0 dtex, and a single fiber fineness of the back layer portion is 4.0 dtex (dtex). A spunbonded nonwoven fabric having a basis weight of 200 g / m 2 was obtained. The results are shown in Table 2.
- Example 9 A fiber web having a single fiber fineness of 2.1 dtex was collected on a moving net conveyor under the same conditions as in Example 3 except that the single fiber fineness was changed by adjusting the discharge amount.
- the fiber web having a single fiber fineness of 6.0 dtex is collected, and the single fiber fineness of the surface layer portion is 2.1 dtex, and the single fiber fineness of the back layer portion is 6.0 dtex.
- a spunbonded nonwoven fabric having a basis weight of 200 g / m 2 was obtained. The results are shown in Table 2.
- Comparative Examples 1, 2, 3, and 7 have the same air flow rate but lack the denseness of the surface layer portion. Dust was easily clogged and the dust removal performance was inferior. Moreover, since the comparative example 4 had a partial recessed part, air permeability was low, it was a high pressure loss, and the dust wiping-off property was unsatisfactory. Moreover, although the comparative example 5 made the structure of the single fiber fineness the same as that of this invention, since it had a partial recessed part, air permeability was low, it was a high-pressure loss, and dust removal property was bad.
- the dust wiping-off property was also unsatisfactory.
- Comparative Example 8 since the single fiber fineness of the surface layer portion was less than 1.5 dtex, although the dust collection rate was good, the air permeability was low and the pressure loss was high.
- Comparative Example 9 since the single fiber fineness of the back layer portion was thicker than 5 dtex, although the air permeability was high and the pressure loss was low, the dust wiping-off property was poor.
- the spunbond nonwoven fabric for filters of the present invention has a small pressure loss and excellent dust collection rate as compared with the spunbond nonwoven fabrics of Comparative Examples 1, 2, 3, and 7. It was excellent in dust removal performance.
- the spunbond nonwoven fabric for filters of the present invention can be suitably used as a pleated filter because it has excellent rigidity, air permeability and dust removal properties. Furthermore, it can be suitably used as a pleated filter base material to be bonded to a filter medium such as a PTFE membrane or nanofiber by utilizing its excellent rigidity and air permeability.
Landscapes
- Engineering & Computer Science (AREA)
- Textile Engineering (AREA)
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Nonwoven Fabrics (AREA)
- Filtering Materials (AREA)
Abstract
Description
高融点ポリエステルの周りに、前記の高融点ポリエステルの融点よりも10~140℃低い融点を有する低融点ポリエステルを配した複合型ポリエステル繊維からなるスパンボンド不織布であって、該スパンボンド不織布は表層部と裏層部を有し、該表層部の複合型ポリエステル繊維の単繊維繊度が1dtex以上3dtex未満、裏層部の単繊維繊度が3dtex以上5dtex以下であり、前記のスパンボンド不織布の目付が130~300g/m2であるフィルター用スパンボンド不織布、である。
下記(a)~(d)の工程を順次施すフィルター用スパンボンド不織布の製造方法、である。
(a)紡糸口金から、高融点ポリエステルの周りに、該高融点ポリエステルの融点よりも10~140℃低い融点を有する低融点ポリエステルを配した複合型ポリエステル繊維を紡出する工程。
(b)紡出された複合型ポリエステル繊維を、高速吸引ガスにより吸引延伸し、移動するネットコンベアー上に捕集して、単繊維繊度1dtex以上3dtex未満の表層部と単繊維繊度3dtex以上5dtex以下の裏層部の複合型ポリエステル繊維からなる繊維ウェブを得る工程。
(c)得られた繊維ウェブに、低融点ポリエステルの融点よりも高く、かつ高融点ポリエステルの融点よりも低い温度の熱風を通過させ、エアスルー熱接着する工程。
(d)前記のエアスルー熱接着された繊維ウェブを、一対のフラットロールまたは2台のベルトコンベアの間に挟み込み、前記の低融点ポリエステルの融点よりも5~75℃低い温度で熱処理し、目付が130~300g/m2のスパンボンド不織布を得る工程。
・見掛け密度(g/cm3)=目付(g/m2)/厚み(mm)/1000
本発明におけるフィルター用スパンボンド不織布の目付あたりの通気量は、0.05~0.50((cm3/cm2・sec)/(g/m2))であることが好ましい。目付あたりの通気量が0.05((cm3/cm2・sec)/(g/m2))以上であると、圧力損失が上昇するのを抑制できる。また、目付あたりの通気量が0.50((cm3/cm2・sec)/(g/m2))以下であると、ダストが内部に滞留しにくいことによりダスト払い落とし性が良好である。より好ましい目付当たりの通気量は0.10~0.48((cm3/cm2・sec)/(g/m2))であり、さらに好ましい目付当たりの通気量は0.15~0.45((cm3/cm2・sec)/(g/m2))である。
本発明におけるフィルター用スパンボンド不織布の目付あたりの剛軟度は、タテ方向とヨコ方向の少なくともどちらか一方が、0.08~0.32((mN)/(g/m2))であることが好ましい。目付あたりの剛軟度が0.08((mN)/(g/m2))以上であると、プリーツ性に優れ、また逆洗時にフィルター用スパンボンド不織布が変形し難くなる。また、目付あたりの剛軟度が0.32(mN)/(g/m2))以下であると、フィルター用スパンボンド不織布を巻き取った際に折れ目が付き難く、高品位となる。
ここで、本発明において、タテ方向とはスパンボンド不織布製造時のシート搬送方向、すなわち不織布ロールにおける巻き取り方向を指し、ヨコ方向とはスパンボンド不織布製造時のシート搬送方向と直交する方向、すなわち不織布ロールにおける幅方向を指すものである。ただし、本発明のスパンボンド不織布の目付あたりの剛軟度は、タテ方向とヨコ方向の少なくともどちらか一方が、0.08~0.32((mN)/(g/m2))であることが好ましく、両方向の測定が可能であれば、シートのタテ方向、ヨコ方向の判別は必要ではない。
上記のとおり、本発明のフィルター用スパンボンド不織布は、上記のように、特定の目付、表裏部の単繊維繊度、見掛け密度、通気量および剛軟度とすることにより、低圧損で、かつダスト払い落とし性にも優れ、従来技術では達成し得なかった長寿命なフィルターとして好適で有用なフィルター用スパンボンド不織布を得ることができる。
(a)紡糸口金から、高融点ポリエステルの周りに、該高融点ポリエステルの融点よりも10~140℃低い融点を有する低融点ポリエステルを配した複合型ポリエステル繊維を紡出する工程。
(b)紡出された複合型ポリエステル繊維を、高速吸引ガスにより吸引延伸し、移動するネットコンベアー上に捕集して、単繊維繊度1dtex以上3dtex未満の表層部と単繊維繊度3dtex以上5dtex以下の裏層部の複合型ポリエステル繊維からなる繊維ウェブを得る工程。
(c)得られた繊維ウェブに、低融点ポリエステルの融点よりも高く、かつ高融点ポリエステルの融点よりも低い温度の熱風を通過させ、エアスルー熱接着する工程。
(d)前記のエアスルー熱接着された繊維ウェブを、一対のフラットロールまたは2台のベルトコンベアの間に挟み込み、前記の低融点ポリエステルの融点よりも5~75℃低い温度で熱処理し、目付が130~300g/m2のスパンボンド不織布を得る工程。
パーキンエルマ社製示差走査型熱量計DSC-2型を用い、昇温速度20℃/分の条件で測定し、得られた融解吸熱曲線において極値を与える温度をポリエステルの融点とした。また、示差走査型熱量計において融解吸熱曲線が極値を示さない樹脂については、ホットプレート上で加熱し、顕微鏡観察により樹脂が溶融した温度を融点とした。
ポリエステルの固有粘度は、次の方法で測定した。
オルソクロロフェノール100mLに対し試料8gを溶解し、温度25℃においてオストワルド粘度計を用いて相対粘度ηrを、下記式により求めた。
(ここで、ηはポリマー溶液の粘度、η0はオルソクロロフェノールの粘度、tは溶液の落下時間(秒)、dは溶液の密度(g/cm3)、t0はオルソクロロフェノールの落下時間(秒)、d0はオルソクロロフェノールの密度(g/cm3)を、それぞれ表す。)
次いで、相対粘度ηrから、下記式により固有粘度IVを算出した。
スパンボンド不織布からランダムに小片サンプル10個を採取し、走査型電子顕微鏡で500~3,000倍の写真を撮影し、各小片サンプルから10本ずつ、計100本の繊維を任意に選び出し、その太さを測定する。繊維は断面が円形と仮定し、太さを繊維径とする。それらの平均値の小数点以下第一位を四捨五入して算出した繊維径とポリマーの密度から単繊維繊度を算出し、小数点第一位を四捨五入して求める。
縦方向50cm×横方向50cmの試料を3個採取して、各試料の質量をそれぞれ測定し、得られた値の平均値を単位面積当たりに換算し、小数点以下第一位を四捨五入した。
厚み計(テクロック社製“TECLOCK”(登録商標)SM-114)を使用して、不織布の厚みを幅方向等間隔に10点測定し、その平均値から小数点以下第3位を四捨五入し、厚みとした。
上記(5)で得られた厚みと上記(4)で得られた目付を用いて、次の式により、見掛け密度を算出し、小数点第3位を四捨五入した。
(7)不織布の通気量(cm3/cm2・sec)
スパンボンド不織布の任意の部分から、10cm×10cmのサンプルを10個採取し、JIS L 1913(2010年度版)に基づき、フラジール形法によって測定した。測定時の設定圧は、125Paとした。通気量は、得られた10点の通気量の平均値を小数点以下第一位を四捨五入して算出する。
上記(7)の通気量で得られた通気量の値を、上記(4)の目付で得られた目付の値で除し、目付当たりの通気量を小数点以下第四位を四捨五入し、算出する。
剛軟度は、JIS L 1913(2010年度版)の6.7.4に記載のガーレ法に準じて測定し、求める。
上記(9)の剛軟度で得られた剛軟度の値を、上記(4)の目付で得られた目付の値で除し、目付あたりの剛軟度を、小数点以下第四位を四捨五入し、算出する。
不織布の引張強力は、JIS L 1913(2010年版)の6.3.1に基づいて、タテ方向とヨコ方向を長辺とした5cm×30cmの試験片を、それぞれ幅方向等間隔に1mあたり3点採取し、定速伸長型引張試験機を用いて、つかみ間隔が20cmで、引張速度が10cm/分の条件で引張試験を実施した。破断したときの強力を読み取り、少数点以下第一位を四捨五入した値を引張強力(N/5cm)とした。
上記(11)の引張強力で得られた引張強力の値を、上記(4)の目付で得られた目付の値で除し、タテ方向とヨコ方向について、それぞれの目付あたりの引張強度を、小数点以下第二位を四捨五入し、算出する。
不織布の任意の部分から、15cm×15cmのサンプルを3個採取し、それぞれの試験装置は、図1に示すように、試験サンプルMをセットするサンプルホルダー1の上流側にダスト供給装置5が連結され、下流側に流量計2、流量調整バルブ3、ブロワ4、およびパルスジェット装置6を連結した構成となっている。試験サンプルの評価面積は、0.01 m2とした。また、サンプルホルダー1に圧力計7が接続されており、試験サンプルMの圧力損失が測定できるようになっている。払い落とし性の試験にあたっては、ダスト供給装置5からJIS15種の標準粉体を20g/m3の濃度になるように供給し、フィルター通過速度が1.5m/分になるように流量調整バルブ3で風量を調整して、ダストを一定濃度で連続的に供給し、試験サンプルMの圧力損失が1,500Paに到達したら、パルスジェット装置6から、0.5MPaの圧縮空気を0.1sec噴射し、試験サンプルMに付着した粉塵(ダスト)を払い落とした。この払い落とし回数が200回に到達するまでの運転時間(hr)をそれぞれ測定し、3回の試験結果の平均値を求め、一の位を四捨五入して運転時間(hr)を求めた。
不織布の任意の部分から、15cm×15cmの試験サンプルを3個採取し、VDI/DIN 3926を参考標準として集塵性能試験を実施した。試験サンプルの濾過面積は0.016 m2とし、濾過風速は2.0m/分とした。ダスト粉塵は、酸化アルミニウム粒子(Dp50:10.5μm)を使用し、試験サンプル上流の粉塵濃度が5g/m3となるよう一定濃度で供給した。
また、30回目の払い落としサイクルの、パルスジェットを噴射してから5秒後の圧力損失を測定し、3回の測定の平均をとり、小数点以下第一位を四捨五入した。
スパンボンド不織布から、ランダムに10mm角の小片サンプル5個を採取し、キーエンス社製ワンショット3D形状測定器VR-3000を用いて、各小片サンプルについて、幅方向4.5mm以上×長手方向4.5mm以上の3D形状測定を行った。続いて、各小片サンプルの両面について、面内の最も高さの高い場所を基準点(深さ0mm)とし、基準点を通る幅方向4.5mmおよび長手方向4.5mmの直線について、直線上に深さが0.1mm以上である部分が、面方向に0.2mm以上連続する箇所(すなわち、深さが0.1mm以上の部分的凹部)の有りと無しを調査した。表1には、いずれの小片サンプルでもこのような深さが0.1mm以上の部分的凹部が存在しない場合は「無し」と記載し、片面にのみ、少なくとも1つの小片サンプルに深さが0.1mm以上の部分的凹部が存在する場合は「片面有り」と記載し、それぞれの面について、少なくとも1つの小片サンプルに深さが0.1mm以上の部分的凹部が存在する場合は「両面有り」と記載した。
水分率50質量ppm以下に乾燥した固有粘度IVが0.65で、融点が260℃のポリエチレンテレフタレート(PET)と、水分率50質量ppm以下に乾燥した固有粘度IVが0.64、イソフタル酸共重合率が11モル%で、融点が230℃の共重合ポリエステル(CO-PET)を、それぞれ295℃と280℃の温度で溶融し、ポリエチレンテレフタレートを芯成分とし、共重合ポリエステルを鞘成分として、口金温度が295℃で、芯:鞘=80:20の質量比率で細孔から紡出した後、エアサッカーにより紡糸速度4,300m/分で円形断面形状のフィラメントを紡糸し、移動するネットコンベアー上に、単繊維繊度が2.1デシテックス(dtex)の繊維ウェブを捕集した上に単繊維繊度が3.4デシテックス(dtex)の繊維ウェブを捕集した。捕集した繊維ウェブに、熱風温度250℃のエアーを通過させた後、一対のフラットロールからなるカレンダーロールによって、温度が180℃で、線圧が50kg/cmの条件で熱接着し、表層部の単繊維繊度が2.1デシテックス(dtex)裏層部の単繊維繊度が3.4デシテックス(dtex)の繊維からなる、目付が200g/m2のスパンボンド不織布を得た。得られたスパンボンド不織布の目付あたりのタテ引張強力は4.3(N/5cm)/(g/m2)であり、目付あたりのヨコ引張強力は3.0(N/5cm)/(g/m2)であった。結果を表1に示す。
ネットコンベアー速度の速度を調整して目付を260g/m2に変更したこと以外は、実施例1と同じ条件で、表層部の単繊維繊度が2.1デシテックス(dtex)裏層部の単繊維繊度が3.4デシテックス(dtex)の繊維からなる、目付が260g/m2のスパンボンド不織布を得た。結果を表1に示す。
水分率50質量ppm以下に乾燥した固有粘度IVが0.65で、融点が260℃のポリエチレンテレフタレート(PET)と、水分率50質量ppm以下に乾燥した固有粘度がIV0.64、イソフタル酸共重合率が11モル%で、融点が230℃の共重合ポリエステル(CO-PET)を、それぞれ295℃と280℃の温度で溶融し、ポリエチレンテレフタレートを芯成分とし、共重合ポリエステルを鞘成分として、口金温度295℃、芯:鞘=80:20の質量比率で細孔から紡出した後、エアサッカーにより紡糸速度4,300m/分で円形断面形状のフィラメントを紡糸し、移動するネットコンベアー上に、単繊維繊度が2.1デシテックス(dtex)の繊維ウェブを捕集した上に単繊維繊度が3.4デシテックス(dtex)の繊維ウェブを捕集した。捕集した繊維ウェブを、熱風温度250℃のエアーを繊維シートに通過させた後、樹脂ベルトからなる2台のベルトコンベアの間に挟み込んで温度170℃の条件下で熱処理し、表層部の単繊維繊度が2.1デシテックス(dtex)裏層部の単繊維繊度が3.4デシテックス(dtex)の繊維からなる、目付が200g/m2のスパンボンド不織布を得た。得られたスパンボンド不織布の目付あたりのタテ引張強力は4.0(N/5cm)/(g/m2)であり、目付あたりのヨコ引張強力は2.7(N/5cm)/(g/m2)であった。結果を表1に示す。
ネットコンベアーの速度を調整して目付を150g/m2に変更したこと以外は、実施例3と同じ条件で、表層部の単繊維繊度が2.1デシテックス(dtex)裏層部の単繊維繊度が3.4デシテックス(dtex)の繊維からなる、目付が150g/m2のスパンボンド不織布を得た。結果を表1に示す。
吐出量を調整して単糸繊維繊度を変更したこと以外は、実施例3と同じ条件で、移動するネットコンベアー上に、単繊維繊度が1.5デシテックス(dtex)の繊維ウェブを捕集した上に単繊維繊度が4.0デシテックス(dtex)の繊維ウェブを捕集して、表層部の単繊維繊度が1.5デシテックス(dtex)裏層部の単繊維繊度が4.0デシテックス(dtex)の繊維からなる、目付が200g/m2のスパンボンド不織布を得た。結果を表1に示す。
単繊維繊度を2.7デシテックスとしたこと以外は、実施例1と同じ条件で、目付が200g/m2のスパンボンド不織布を得た。得られたスパンボンド不織布の目付あたりのタテ引張強力は4.4(N/5cm)/(g/m2)であり、目付あたりのヨコ引張強力は3.1(N/5cm)/(g/m2)であった。結果を表2に示す。
ネットコンベアー速度の速度を調整して目付を260g/m2に変更したこと以外は、実施例1と同じ条件で単繊維繊度が2.7デシテックスの繊維からなる、目付が260g/m2のスパンボンド不織布を得た。結果を表2に示す。
熱風温度250℃のエアーを繊維シートに通過させた後、樹脂ベルトからなる2台のベルトコンベアの間に挟み込んで温度170℃の条件下で熱処理したこと以外は、実施例1と同じ条件で、単繊維繊度が2.7デシテックスの繊維からなる、目付が200g/m2のスパンボンド不織布を得た。結果を表2に示す。
水分率50質量ppm以下に乾燥した固有粘度IVが0.65で、融点が260℃のポリエチレンテレフタレート(PET)と、水分率50質量ppm以下に乾燥した固有粘度IV0.64、イソフタル酸共重合率11モル%で融点230℃の共重合ポリエステル(CO-PET)を、それぞれ295℃と280℃の温度で溶融し、ポリエチレンテレフタレートを芯成分とし、共重合ポリエステルを鞘成分として、口金温度295℃、芯:鞘=80:20の質量比率で細孔から紡出した後、圧着面積率18%となるエンボスロールで、温度が200℃で、線圧が60kg/cmの条件で熱接着し、単繊維繊度が2.7デシテックスの繊維からなる、目付が200g/m2のスパンボンド不織布を得た。結果を表2に示す。
移動するネットコンベアー上に、単繊維繊度が2.1デシテックス(dtex)の繊維ウェブを捕集した上に単繊維繊度が3.4デシテックス(dtex)の繊維ウェブを捕集して、表層部の単繊維繊度が2.1デシテックス(dtex)裏層部の単繊維繊度が3.4デシテックス(dtex)の繊維としたこと以外は、比較例4と同じ条件で圧着面積率18%となるエンボスロールで、温度が200℃で、線圧が60kg/cmの条件で熱接着し、目付が200g/m2のスパンボンド不織布を得た。結果を表2に示す。
ネットコンベアー速度の速度を調整して目付を260g/m2に変更し、圧着面積率10%となるエンボスロールで熱接着したこと以外は比較例5と同じ条件で、表層部の単繊維繊度が2.1デシテックス(dtex)裏層部の単繊維繊度が3.4デシテックス(dtex)の繊維からなる、目付が260g/m2のスパンボンド不織布を得た。結果を表2に示す。
ネットコンベアー速度の速度を調整して目付を150g/m2に変更したこと以外は、実施例3と同じ条件で単繊維繊度が2.7デシテックスの繊維からなる、目付が150g/m2のスパンボンド不織布を得た。結果を表2に示す。
吐出量を調整して単繊維繊度を変更したこと以外は、実施例3と同じ条件で、移動するネットコンベアー上に、単繊維繊度が0.8デシテックス(dtex)の繊維ウェブを捕集した上に単繊維繊度が4.5デシテックス(dtex)の繊維ウェブを捕集して、表層部の単繊維繊度が1.0デシテックス(dtex)裏層部の単繊維繊度が4.0デシテックス(dtex)の繊維からなる、目付が200g/m2のスパンボンド不織布を得た。結果を表2に示す。
吐出量を調整して単繊維繊度を変更したこと以外は、実施例3と同じ条件で、移動するネットコンベアー上に、単繊維繊度が2.1デシテックス(dtex)の繊維ウェブを捕集した上に単繊維繊度が6.0デシテックス(dtex)の繊維ウェブを捕集して、表層部の単繊維繊度が2.1デシテックス(dtex)裏層部の単繊維繊度が6.0デシテックス(dtex)の繊維からなる、目付が200g/m2のスパンボンド不織布を得た。結果を表2に示す。
2:流量計
3:流量調整バルブ
4:ブロワ
5:ダスト供給装置
6:パルスジェット装置
7:圧力計
M:測定サンプル
Claims (7)
- 高融点ポリエステルの周りに、前記高融点ポリエステルの融点よりも10~140℃低い融点を有する低融点ポリエステルを配した複合型ポリエステル繊維からなるスパンボンド不織布であって、該スパンボンド不織布は表層部と裏層部を有し、該表層部の複合型ポリエステル繊維の単繊維繊度が1dtex以上3dtex未満、裏層部の単繊維繊度が3dtex以上5dtex以下であり、前記スパンボンド不織布の目付が130~300g/m2であるフィルター用スパンボンド不織布。
- 複合型ポリエステル繊維の複合形態が、高融点ポリエステルを芯成分とし、低融点ポリエステルを鞘成分とする芯鞘型であり、かつ、前記芯成分と前記鞘成分の芯鞘成分質量比率が90:10~60:40である請求項1に記載のフィルター用スパンボンド不織布。
- 少なくとも一方の表面に深さ0.1mm以上の部分的凹部がない請求項1または2のいずれかに記載のフィルター用スパンボンド不織布。
- 高融点ポリエステルがポリエチレンテレフタレートであり、かつ低融点ポリエステルが共重合ポリエチレンテレフタレートである請求項1~3のいずれかに記載のフィルター用スパンボンド不織布。
- 下記(a)~(d)の工程を順次施すフィルター用スパンボンド不織布の製造方法。
(a)紡糸口金から、高融点ポリエステルの周りに、前記高融点ポリエステルの融点よりも10~140℃低い融点を有する低融点ポリエステルを配した複合型ポリエステル繊維を紡出する工程。
(b)紡出された複合型ポリエステル繊維を、高速吸引ガスにより吸引延伸し、移動するネットコンベアー上に捕集して、単繊維繊度が1dtex以上3dtex未満の表層部と単繊維繊度が3dtex以上5dtex以下の裏層部の複合型ポリエステル繊維からなる繊維ウェブを得る工程。
(c)得られた繊維ウェブに、前記低融点ポリエステルの融点よりも高く、かつ前記高融点ポリエステルの融点よりも低い温度の熱風を通過させ、エアスルー熱接着する工程。
(d)前記エアスルー熱接着された繊維ウェブを、一対のフラットロールまたは2台のベルトコンベアの間に挟み込み、前記の低融点ポリエステルの融点よりも5~75℃低い温度で熱処理し、目付が130~300g/m2のスパンボンド不織布を得る工程。 - 複合型ポリエステル繊維の複合形態が、高融点ポリエステルを芯成分とし、低融点ポリエステルを鞘成分とする芯鞘型であり、かつ、前記芯成分と前記鞘成分の芯鞘成分質量比率が90:10~60:40である請求項5に記載のフィルター用スパンボンド不織布の製造方法。
- 高融点ポリエステルがポリエチレンテレフタレートであり、かつ低融点ポリエステルが共重合ポリエチレンテレフタレートである請求項5または6に記載のフィルター用スパンボンド不織布の製造方法。
Priority Applications (5)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201880024737.3A CN110494201A (zh) | 2017-05-30 | 2018-05-07 | 过滤器用纺粘无纺布及其制造方法 |
JP2018524846A JP7180376B2 (ja) | 2017-05-30 | 2018-05-07 | フィルター用スパンボンド不織布の製造方法 |
KR1020197032854A KR20200014743A (ko) | 2017-05-30 | 2018-05-07 | 필터용 스펀본드 부직포 및 그의 제조 방법 |
US16/613,872 US20200139282A1 (en) | 2017-05-30 | 2018-05-07 | Spunbond non-woven fabric for filter and method of manufacturing said fabric |
EP18809935.2A EP3632524A4 (en) | 2017-05-30 | 2018-05-07 | SPINNED FABRIC FOR FILTERS AND METHOD OF MANUFACTURING THEREOF |
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2017-106243 | 2017-05-30 | ||
JP2017106243 | 2017-05-30 |
Publications (1)
Publication Number | Publication Date |
---|---|
WO2018221122A1 true WO2018221122A1 (ja) | 2018-12-06 |
Family
ID=64456269
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
PCT/JP2018/017617 WO2018221122A1 (ja) | 2017-05-30 | 2018-05-07 | フィルター用スパンボンド不織布およびその製造方法 |
Country Status (6)
Country | Link |
---|---|
US (1) | US20200139282A1 (ja) |
EP (1) | EP3632524A4 (ja) |
JP (1) | JP7180376B2 (ja) |
KR (1) | KR20200014743A (ja) |
CN (1) | CN110494201A (ja) |
WO (1) | WO2018221122A1 (ja) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2021132409A1 (ja) * | 2019-12-23 | 2021-07-01 | 東レ株式会社 | フィルター用スパンボンド不織布、粉体塗装フィルター用濾材および粉体塗装フィルター |
Families Citing this family (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2021132410A1 (ja) * | 2019-12-23 | 2021-07-01 | 東レ株式会社 | スパンボンド不織布、集塵機プリーツフィルター用濾材、集塵機プリーツフィルターおよび大風量パルスジェットタイプ集塵機 |
CN114829691B (zh) * | 2019-12-23 | 2024-02-02 | 东丽株式会社 | 纺粘无纺布、集尘器褶皱过滤器用滤材及过滤器、集尘器 |
JP2021183297A (ja) * | 2020-05-20 | 2021-12-02 | セイコーエプソン株式会社 | シート状フィルター、マスクおよびシート製造装置 |
CN112221250B (zh) * | 2020-09-10 | 2022-03-22 | 青岛中亚环保工程有限公司 | 一种pbs/pp双组份熔喷纤维过滤材料及其制造方法 |
WO2022065191A1 (ja) * | 2020-09-28 | 2022-03-31 | 東洋紡株式会社 | 長繊維不織布、及び、長繊維不織布の製造方法 |
KR102342025B1 (ko) * | 2021-05-11 | 2021-12-23 | 남양부직포 주식회사 | 복합필터여재용 열융착 필터지지체, 이를 포함하는 복합필터여재 및 이를 포함하는 마스크 |
Citations (12)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS534043B2 (ja) | 1975-06-30 | 1978-02-14 | ||
JPS5353076A (en) * | 1976-10-25 | 1978-05-15 | Matsushita Electric Ind Co Ltd | Filter for vacuum cleaner |
JPS558858A (en) * | 1978-07-07 | 1980-01-22 | Toray Ind Inc | Dust collection filter |
JPS6490135A (en) | 1987-08-22 | 1989-04-06 | British Petroleum Co | Asymmetric synthesis of carboxylic acid ester and/or carboxylic acid |
JPH01192406A (ja) | 1988-01-25 | 1989-08-02 | Kubota Ltd | 黒鉛を有する高クロムロール |
JPH07157960A (ja) | 1993-12-06 | 1995-06-20 | Toyobo Co Ltd | 寸法安定性に優れた長繊維不織布及びその防水製品 |
JPH1190135A (ja) * | 1997-09-25 | 1999-04-06 | Chisso Corp | プリーツフィルター |
US6090731A (en) * | 1994-10-31 | 2000-07-18 | Kimberly-Clark Worldwide, Inc. | High density nonwoven filter media |
JP2004019061A (ja) * | 2002-06-18 | 2004-01-22 | Toyobo Co Ltd | ポリエステル系複合不織布およびフィルター |
JP2006150222A (ja) * | 2004-11-29 | 2006-06-15 | Daiwabo Co Ltd | 筒状フィルター及びその製造方法 |
JP2008151980A (ja) * | 2006-12-18 | 2008-07-03 | Mahle Filter Systems Japan Corp | トナーフィルター用濾材とその濾材を用いたカセットフィルター |
JP2009006318A (ja) | 2007-05-31 | 2009-01-15 | Toray Ind Inc | 円筒状バグフィルター |
Family Cites Families (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS534043A (en) | 1976-03-06 | 1978-01-14 | Dainippon Toryo Co Ltd | Water-dispersible, thermosetting coating compositions |
US5443606A (en) * | 1992-03-26 | 1995-08-22 | The University Of Tennessee Reserch Corporation | Post-treatment of laminated nonwoven cellulosic fiber webs |
US5670044A (en) * | 1993-05-04 | 1997-09-23 | Chisso Corporation | Cylindrical filter and process for producing the same |
JP3744232B2 (ja) | 1997-10-30 | 2006-02-08 | 東レ株式会社 | フィルター用基材およびフィルター装置 |
WO2007088824A1 (ja) * | 2006-02-01 | 2007-08-09 | Toray Industries, Inc. | フィルター用不織布およびその製造方法 |
JP5508858B2 (ja) * | 2007-12-12 | 2014-06-04 | 株式会社きもと | ニュートンリング防止シート、及びこれを用いたタッチパネル |
JP5353076B2 (ja) * | 2008-06-11 | 2013-11-27 | パナソニック株式会社 | 成形方法および金型装置 |
JP5477123B2 (ja) * | 2010-04-02 | 2014-04-23 | Jnc株式会社 | 熱風処理不織布加工装置および加工方法 |
CN102451589B (zh) * | 2010-11-02 | 2015-09-09 | 东丽纤维研究所(中国)有限公司 | 一种耐热性过滤材料及其生产方法和用途 |
-
2018
- 2018-05-07 US US16/613,872 patent/US20200139282A1/en not_active Abandoned
- 2018-05-07 JP JP2018524846A patent/JP7180376B2/ja active Active
- 2018-05-07 EP EP18809935.2A patent/EP3632524A4/en not_active Withdrawn
- 2018-05-07 WO PCT/JP2018/017617 patent/WO2018221122A1/ja active Application Filing
- 2018-05-07 KR KR1020197032854A patent/KR20200014743A/ko not_active Application Discontinuation
- 2018-05-07 CN CN201880024737.3A patent/CN110494201A/zh active Pending
Patent Citations (12)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS534043B2 (ja) | 1975-06-30 | 1978-02-14 | ||
JPS5353076A (en) * | 1976-10-25 | 1978-05-15 | Matsushita Electric Ind Co Ltd | Filter for vacuum cleaner |
JPS558858A (en) * | 1978-07-07 | 1980-01-22 | Toray Ind Inc | Dust collection filter |
JPS6490135A (en) | 1987-08-22 | 1989-04-06 | British Petroleum Co | Asymmetric synthesis of carboxylic acid ester and/or carboxylic acid |
JPH01192406A (ja) | 1988-01-25 | 1989-08-02 | Kubota Ltd | 黒鉛を有する高クロムロール |
JPH07157960A (ja) | 1993-12-06 | 1995-06-20 | Toyobo Co Ltd | 寸法安定性に優れた長繊維不織布及びその防水製品 |
US6090731A (en) * | 1994-10-31 | 2000-07-18 | Kimberly-Clark Worldwide, Inc. | High density nonwoven filter media |
JPH1190135A (ja) * | 1997-09-25 | 1999-04-06 | Chisso Corp | プリーツフィルター |
JP2004019061A (ja) * | 2002-06-18 | 2004-01-22 | Toyobo Co Ltd | ポリエステル系複合不織布およびフィルター |
JP2006150222A (ja) * | 2004-11-29 | 2006-06-15 | Daiwabo Co Ltd | 筒状フィルター及びその製造方法 |
JP2008151980A (ja) * | 2006-12-18 | 2008-07-03 | Mahle Filter Systems Japan Corp | トナーフィルター用濾材とその濾材を用いたカセットフィルター |
JP2009006318A (ja) | 2007-05-31 | 2009-01-15 | Toray Ind Inc | 円筒状バグフィルター |
Non-Patent Citations (1)
Title |
---|
See also references of EP3632524A4 |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2021132409A1 (ja) * | 2019-12-23 | 2021-07-01 | 東レ株式会社 | フィルター用スパンボンド不織布、粉体塗装フィルター用濾材および粉体塗装フィルター |
Also Published As
Publication number | Publication date |
---|---|
US20200139282A1 (en) | 2020-05-07 |
EP3632524A4 (en) | 2021-03-10 |
KR20200014743A (ko) | 2020-02-11 |
JP7180376B2 (ja) | 2022-11-30 |
JPWO2018221122A1 (ja) | 2020-03-26 |
EP3632524A1 (en) | 2020-04-08 |
CN110494201A (zh) | 2019-11-22 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
WO2017110365A1 (ja) | フィルター用スパンボンド不織布およびその製造方法 | |
WO2018221122A1 (ja) | フィルター用スパンボンド不織布およびその製造方法 | |
KR101441593B1 (ko) | 필터용 부직포 및 그 제조 방법 | |
JP4852104B2 (ja) | 耐熱性不織布 | |
US8308833B2 (en) | Nonwoven fabric for filters | |
JP5082365B2 (ja) | フィルター用不織布 | |
JP6669315B1 (ja) | フィルター用スパンボンド不織布およびその製造方法 | |
JP2007152216A (ja) | フィルター用不織布 | |
JP6962494B1 (ja) | スパンボンド不織布、フィルター積層濾材、集塵機プリーツフィルター用濾材、集塵機プリーツフィルターおよび中風量パルスジェットタイプ集塵機 | |
JP2010121241A (ja) | フィルター用不織布 | |
JP6658113B2 (ja) | エアクリーナー用不織布 | |
JP2019000793A (ja) | 集塵機フィルター用濾過材 | |
KR101242687B1 (ko) | 폴리에스테르계 부직포 및 이의 제조 방법 | |
JP2013544975A (ja) | 高均一性スパンボンド不織布 | |
JP2020196963A (ja) | メルトブロー不織布および耐熱フィルター積層体ならびにそれらの製造方法 | |
JP2007237167A (ja) | フィルター用不織布 | |
WO2021132411A1 (ja) | スパンボンド不織布、フィルター積層濾材、プリーツフィルター用濾材およびプリーツフィルター | |
JP2021098930A (ja) | スパンボンド不織布、集塵機プリーツフィルター用濾材、集塵機プリーツフィルターおよび大風量パルスジェットタイプ集塵機 | |
JP2022132085A (ja) | 積層不織布、フィルター用濾材、集塵機用プリーツフィルター、ならびに、パルスジェットタイプ集塵機 | |
KR20220110210A (ko) | 스펀본드 부직포, 집진기 플리츠 필터용 여과재, 집진기 플리츠 필터 및 대풍량 펄스제트 타입 집진기 | |
KR20230101133A (ko) | 여과성능이 향상된 부직포 및 이의 제조방법 | |
KR20220112773A (ko) | 스펀본드 부직포, 집진기 플리츠 필터용 여과재, 집진기 플리츠 필터 및 대풍량 펄스제트 타입 집진기 |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
ENP | Entry into the national phase |
Ref document number: 2018524846 Country of ref document: JP Kind code of ref document: A |
|
121 | Ep: the epo has been informed by wipo that ep was designated in this application |
Ref document number: 18809935 Country of ref document: EP Kind code of ref document: A1 |
|
ENP | Entry into the national phase |
Ref document number: 20197032854 Country of ref document: KR Kind code of ref document: A |
|
NENP | Non-entry into the national phase |
Ref country code: DE |
|
WWE | Wipo information: entry into national phase |
Ref document number: 2018809935 Country of ref document: EP |
|
ENP | Entry into the national phase |
Ref document number: 2018809935 Country of ref document: EP Effective date: 20200102 |