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WO2019187827A1 - Nonwoven fabric, method for forming fiber, method for manufacturing nonwoven fabric - Google Patents

Nonwoven fabric, method for forming fiber, method for manufacturing nonwoven fabric Download PDF

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Publication number
WO2019187827A1
WO2019187827A1 PCT/JP2019/006503 JP2019006503W WO2019187827A1 WO 2019187827 A1 WO2019187827 A1 WO 2019187827A1 JP 2019006503 W JP2019006503 W JP 2019006503W WO 2019187827 A1 WO2019187827 A1 WO 2019187827A1
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WO
WIPO (PCT)
Prior art keywords
fiber
nonwoven fabric
collector
solvent
nozzle
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Ceased
Application number
PCT/JP2019/006503
Other languages
French (fr)
Japanese (ja)
Inventor
洋亮 中川
金村 一秀
竜太 竹上
邦行 神長
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Fujifilm Corp
Original Assignee
Fujifilm Corp
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Fujifilm Corp filed Critical Fujifilm Corp
Priority to KR1020207027759A priority Critical patent/KR102411467B1/en
Priority to CN201980021814.4A priority patent/CN111918993B/en
Priority to JP2020510432A priority patent/JPWO2019187827A1/en
Publication of WO2019187827A1 publication Critical patent/WO2019187827A1/en
Anticipated expiration legal-status Critical
Ceased legal-status Critical Current

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Classifications

    • DTEXTILES; PAPER
    • D04BRAIDING; LACE-MAKING; KNITTING; TRIMMINGS; NON-WOVEN FABRICS
    • D04HMAKING 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
    • D04H1/00Non-woven fabrics formed wholly or mainly of staple fibres or like relatively short fibres
    • D04H1/40Non-woven fabrics formed wholly or mainly of staple fibres or like relatively short fibres from fleeces or layers composed of fibres without existing or potential cohesive properties
    • D04H1/42Non-woven fabrics formed wholly or mainly of staple fibres or like relatively short fibres from fleeces or layers composed of fibres without existing or potential cohesive properties characterised by the use of certain kinds of fibres insofar as this use has no preponderant influence on the consolidation of the fleece
    • D04H1/4382Stretched reticular film fibres; Composite fibres; Mixed fibres; Ultrafine fibres; Fibres for artificial leather
    • D04H1/43838Ultrafine fibres, e.g. microfibres
    • DTEXTILES; PAPER
    • D01NATURAL OR MAN-MADE THREADS OR FIBRES; SPINNING
    • D01DMECHANICAL METHODS OR APPARATUS IN THE MANUFACTURE OF ARTIFICIAL FILAMENTS, THREADS, FIBRES, BRISTLES OR RIBBONS
    • D01D5/00Formation of filaments, threads, or the like
    • D01D5/0007Electro-spinning
    • D01D5/0015Electro-spinning characterised by the initial state of the material
    • D01D5/003Electro-spinning characterised by the initial state of the material the material being a polymer solution or dispersion
    • DTEXTILES; PAPER
    • D01NATURAL OR MAN-MADE THREADS OR FIBRES; SPINNING
    • D01DMECHANICAL METHODS OR APPARATUS IN THE MANUFACTURE OF ARTIFICIAL FILAMENTS, THREADS, FIBRES, BRISTLES OR RIBBONS
    • D01D5/00Formation of filaments, threads, or the like
    • D01D5/04Dry spinning methods
    • DTEXTILES; PAPER
    • D04BRAIDING; LACE-MAKING; KNITTING; TRIMMINGS; NON-WOVEN FABRICS
    • D04HMAKING 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
    • D04H1/00Non-woven fabrics formed wholly or mainly of staple fibres or like relatively short fibres
    • D04H1/40Non-woven fabrics formed wholly or mainly of staple fibres or like relatively short fibres from fleeces or layers composed of fibres without existing or potential cohesive properties
    • D04H1/42Non-woven fabrics formed wholly or mainly of staple fibres or like relatively short fibres from fleeces or layers composed of fibres without existing or potential cohesive properties characterised by the use of certain kinds of fibres insofar as this use has no preponderant influence on the consolidation of the fleece
    • D04H1/425Cellulose series
    • D04H1/4258Regenerated cellulose series
    • DTEXTILES; PAPER
    • D04BRAIDING; LACE-MAKING; KNITTING; TRIMMINGS; NON-WOVEN FABRICS
    • D04HMAKING 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
    • D04H1/00Non-woven fabrics formed wholly or mainly of staple fibres or like relatively short fibres
    • D04H1/70Non-woven fabrics formed wholly or mainly of staple fibres or like relatively short fibres characterised by the method of forming fleeces or layers, e.g. reorientation of fibres
    • D04H1/72Non-woven fabrics formed wholly or mainly of staple fibres or like relatively short fibres characterised by the method of forming fleeces or layers, e.g. reorientation of fibres the fibres being randomly arranged
    • D04H1/728Non-woven fabrics formed wholly or mainly of staple fibres or like relatively short fibres characterised by the method of forming fleeces or layers, e.g. reorientation of fibres the fibres being randomly arranged by electro-spinning

Definitions

  • the present invention relates to a nonwoven fabric, a fiber forming method, and a nonwoven fabric manufacturing method.
  • Nonwoven fabrics made of fiber are known.
  • the fiber include a so-called nanofiber having a nano-order diameter of several nm or more and less than 1000 nm, and a so-called micron fiber having a diameter of several micrometers or more and less than 1000 ⁇ m.
  • a fiber structure including a layer made of fibers such as nonwoven fabric for example, in Patent Document 1, it is used as a separator or an insulating material in a battery or the like, and has a high average diameter of 50 nm to 3000 nm.
  • a fiber structure comprising a fiber layer made of molecular fibers is described. This fiber structure has a maximum compression rate of 20% or more at a surface pressure of 5 MPa measured by a predetermined method.
  • the fiber layer has an average pore diameter of 0.01 to 15 ⁇ m, a thickness of 0.0025 to 0.3 mm, a porosity of 20 to 90%, a weighing of 1 to 90 g / m 2 , and a fragile air permeability of 46 m 3 / min / m. It is less than 2 and the Macmillan number is 2-15.
  • an electrospinning method is known as a method for producing a fiber such as a nanofiber and a non-woven fabric formed of such a fiber.
  • the electrospinning method is also referred to as an electrospinning method or the like, and is performed using, for example, an electrospinning device (also referred to as an electrospinning device) having a nozzle, a collector, and a power source.
  • an electrospinning device also referred to as an electrospinning device having a nozzle, a collector, and a power source.
  • a voltage is applied between a nozzle and a collector by a power source, and for example, the nozzle is negatively charged and the collector is positively charged.
  • Nonwoven fabrics made of nanofibers and micronfibers have been actively developed in various fields. Expected uses include, for example, a heat insulating material, a sound absorbing material, a filter, and the like, and are expected to be used as a medical nonwoven fabric.
  • the porosity of the fiber layer for favorably absorbing the electrolyte, ions flow between the anode and the cathode.
  • the thickness for facilitating the measurement and the weighing for preventing the dendride short between the anode and the cathode are specified. Therefore, for example, the sound absorbing material and the heat insulating material are difficult to develop in the above-mentioned applications such as insufficient sound absorbing performance and heat insulating performance.
  • a non-woven fabric having a fluffy feeling that is, a soft non-woven fabric that wraps a large amount of air, has sound absorption performance, heat insulation performance, and the like, and can be expected to expand its application.
  • an object of the present invention is to provide a nonwoven fabric having a fluffy feeling, a fiber forming method for obtaining the nonwoven fabric, and a nonwoven fabric manufacturing method.
  • the nonwoven fabric of the present invention comprises a fiber having an average diameter in the range of 0.10 ⁇ m to 5.0 ⁇ m, a porosity of at least 90%, and an average pore diameter in the range of 0.5 ⁇ m to 50 ⁇ m, And even if the standard deviation of a hole diameter is large, it is 1.5 micrometers.
  • the fiber is preferably formed of a cellulosic polymer.
  • a fiber is formed by applying a voltage between a solution in which a fiber material is dissolved in a solvent and the collector, and ejecting the solution from the nozzle to the collector.
  • the evaporation rate of the solvent is V ⁇ l / s and the average diameter of the fiber is DF ⁇ m, 1 ⁇ V / DF ⁇ 10.
  • the moisture content of the fiber is at least 3.0%.
  • the spinning space is preferably partitioned from the external space by a chamber having a humidity adjusting mechanism for adjusting the internal relative humidity.
  • the fiber material is preferably a cellulosic polymer.
  • the cellulosic polymer is preferably cellulose acylate.
  • the cellulose acylate is preferably either cellulose acetate propionate or cellulose triacetate.
  • the solvent is preferably a mixture of a plurality of compounds.
  • the solvent preferably contains dichloromethane and methanol.
  • the non-woven fabric production method of the present invention collects fibers formed by applying a voltage between a solution in which a fiber material is dissolved in a solvent and a collector and ejecting the solution from a nozzle as a non-woven fabric on the collector. To do.
  • the evaporation rate of the solvent is V ⁇ l / s and the average diameter of the fiber is DF ⁇ m, 1 ⁇ V / DF ⁇ 10.
  • a nonwoven fabric with a fluffy feeling can be obtained.
  • the nonwoven fabric 10 of this embodiment shown in FIG. In the nonwoven fabric 10, a plurality of voids 13 as space regions defined by the fibers 11 are formed as portions where air exists. Thus, the nonwoven fabric 10 contains air inside.
  • a first surface 10 ⁇ / b> A side in the thickness direction Z of the nonwoven fabric 10 is drawn in order to avoid complication of the drawing. Therefore, the nonwoven fabric 10 has a structure in which a large number of fibers 11 are further stacked on the lower side in FIG.
  • the holes When the plurality of voids 13 communicate with each other in the thickness direction Z of the nonwoven fabric 10, holes that penetrate in the thickness direction Z of the nonwoven fabric 10 are formed.
  • the holes function as filter holes when the nonwoven fabric 10 is used for a filter, for example.
  • some of the gaps 13 exist as a space region that does not penetrate in the thickness direction Z, for example, is closed by the fiber 11 without forming holes.
  • the nonwoven fabric 10 only needs to include the fiber 11, and may include other fibers having different materials in addition to the fiber 11.
  • the first surface 10 ⁇ / b> A is drawn along the XY plane, and Z perpendicular to the XY plane is the thickness direction of the nonwoven fabric 10.
  • the fiber 11 is formed with a substantially constant diameter D1.
  • the average value of diameter D1 (hereinafter referred to as average diameter) DF (unit: ⁇ m) is preferably in the range of 0.10 ⁇ m or more and 5.00 ⁇ m or less.
  • the suppression of the fiber piece detachment means that the fiber piece detachment from the nonwoven fabric 10 is suppressed, and the suppression of the fiber piece detachment leads to excellent durability as the nonwoven fabric 10. .
  • the nonwoven fabric 10 Since the average diameter DF is 5.00 ⁇ m or less, the nonwoven fabric 10 has the same volume ratio of air (hereinafter referred to as porosity) compared to the case where the average diameter DF is larger than 5.00 ⁇ m. It becomes softer. Further, when the average diameter DF is 5.00 ⁇ m or less, the non-woven fabric 10 has a higher porosity even if the nonwoven fabric 10 has the same degree of softness as compared with the case where the average diameter DF is larger than 5.00 ⁇ m. When used as a material or a heat insulating material, the sound absorbing performance and the heat insulating performance are increased, and the amount of filtration treatment when used for a filter is increased.
  • the diameter is more preferably in the range of 0.15 ⁇ m to 4.00 ⁇ m, and still more preferably in the range of 0.20 ⁇ m to 3.00 ⁇ m.
  • the average diameter DF can be obtained by measuring the diameter of 100 fibers 11 from an image taken with a scanning electron microscope and calculating the average value.
  • the nonwoven fabric 10 has a porosity of 90% or more, that is, at least 90%.
  • the nonwoven fabric 10 with a very high porosity has a fluffy feeling. That is, it contains a large amount of air inside and is soft. Since it contains a large amount of air in this way, it has a wider range of uses than when it has a porosity of less than 90%.
  • the sound absorption performance and heat insulation performance superior to the case of a porosity of less than 90% are exhibited, it can be used as a sound absorption material and a heat insulation material.
  • a big filtration processing performance is shown.
  • the filtration performance means the treatment amount per unit time and / or the sustainability of a state where clogging is suppressed.
  • using as a filter may be more preferable.
  • the porosity is preferably 99.8% or less because higher durability as the nonwoven fabric 10 is secured.
  • the porosity is more preferably in the range of 90% or more and 99.8% or less, further preferably in the range of 95% or more and 99.6% or less, and particularly preferably 97% or more and 99.4% or less. Within range.
  • the porosity (unit:%) is W (unit: g / m 2 ), the thickness is H (unit: mm), and the specific gravity of the fiber 11 is ⁇ 1 (unit: kg / m 3 ). Then, [1- ⁇ (W / 1000) / (H / 1000) ⁇ / ⁇ 1] ⁇ 100 can be obtained.
  • the nonwoven fabric 10 is cut into 5 cm ⁇ 5 cm, the mass is measured with an electronic balance (manufactured by METTLER TOLEDO), and a value obtained by converting the measured value per 1 m 2 is used.
  • the thickness H is measured by a non-contact laser displacement meter (LK-H025 manufactured by Keyence Corporation).
  • the fibers 11 are intertwined, and it is preferable that a portion overlapping in the thickness direction Z and / or a portion contacting in the surface direction (in the XY plane) of the nonwoven fabric 10 is not bonded (not bonded). This is the case in the example. However, there may be a part where the bonding is performed, and even when the bonding is performed, the bonding force is kept small enough to be easily peeled off by a very weak force. As described above, the fibers 11 are intertwined with each other, or even if they are bonded, the adhesive force is suppressed to be small. Therefore, the fibers 11 are soft and deformable in a state of containing a large amount of air.
  • the degree of freedom of construction site is large. Further, since the fibers 11 are in an intertwined state, or the adhesive force is kept small even if they are bonded, when the fiber 11 has a small diameter of, for example, 0.10 ⁇ m or more and 5.00 ⁇ m or less, It can also be torn by applying tension locally. Therefore, it is excellent in workability.
  • the thickness of the nonwoven fabric 10 is not particularly limited, and can be adjusted according to the amount of fiber 11 deposited as described later, and may be set as appropriate according to the handling situation and / or application. For example, from the viewpoint of handleability (handling) such as workability and durability in handling scenes, it is preferably in the range of 100 ⁇ m to 100,000 ⁇ m, for example. Further, when used as a sound absorbing material or a heat insulating material, it may be thickened (for example, within a range of 2000 ⁇ m or more and 100,000 ⁇ m or less) to be applied as it is, or thinned (for example, to be applied in a stacked state) It may be within a range of 200 ⁇ m or more and 1000 ⁇ m or less. In this example, it is 4000 ⁇ m. Although the nonwoven fabric 10 has a large degree of freedom in thickness as described above, it contains a large amount of air and is soft, and therefore has a wide range of uses.
  • the average pore diameter of the nonwoven fabric 10 in which a plurality of voids 13 are formed is DA (unit: ⁇ m).
  • the average pore diameter DA is in the range of 0.5 ⁇ m to 50 ⁇ m, and the standard deviation of the pore diameter is 1.5 ⁇ m or less, that is, 1.5 ⁇ m at most.
  • the average pore diameter DA is more preferably in the range of 2 ⁇ m to 30 ⁇ m, and still more preferably in the range of 4 ⁇ m to 20 ⁇ m.
  • the standard deviation of the pore diameter is more preferably 1.0 ⁇ m or less, further preferably 0.5 ⁇ m or less, and it is more preferable that the pore size is kept small.
  • the average pore diameter DA can be obtained by the following method. First, a 5 cm square (5 cm ⁇ 5 cm) is cut out from the fiber sheet 10 to obtain a sample. After immersing this sample in GALWICK (manufactured by POROUS MATERIAL) having a surface tension of 15.3 mN / m, the average pore diameter DA is determined by measuring by a bubble point method using a palm porometer (manufactured by POROUS MATERIAL). can get.
  • GALWICK manufactured by POROUS MATERIAL
  • the standard deviation of the hole diameter is obtained by the following method using the hole diameter distribution (correlation data between the hole diameter and the abundance of holes having the hole diameter) output from the palm porometer.
  • the total amount of holes is 100%. . This is referred to as a total amount of 100%.
  • the corresponding vertical axis is the right vertical axis in FIG.
  • the fiber 11 is made of resin (polymer).
  • a polymer that can be made into a solution by dissolving in a solvent is used.
  • the polymer is preferably a polymer that can be made into a solution by dissolving in an organic solvent. Examples thereof include polymethyl methacrylate (hereinafter referred to as PMMA), cellulosic polymer, polyester, polyurethane, and elastomer.
  • PMMA polymethyl methacrylate
  • cellulosic polymer polyester, polyurethane, and elastomer.
  • a cellulose polymer 15 see FIG. 3 is used.
  • the cellulose polymer 15 is preferably cellulose acylate.
  • Cellulose acylate is a cellulose ester in which some or all of the hydrogen atoms constituting the hydroxy group of cellulose are substituted with acyl groups.
  • the cellulose acylate is preferably any one of cellulose acetate propionate (hereinafter referred to as CAP) and cellulose triacetate (hereinafter referred to as TAC).
  • the average pore size distribution is narrow, it can be suitably used as a filter for separating or removing a target substance from a mixture of solid and liquid (solid liquid mixture).
  • filters that can be particularly preferably used are for food (including beverages), medical, and ultrapure, where there is concern about contamination (contamination) and high precision separation performance is required. It is a filter for water and high-purity chemicals. Due to the fluffy feeling and the high porosity, it is difficult to clog and the pressure loss is small.
  • Specific examples include a filter for removing fine particles and / or microorganisms from beverages, a pretreatment filter for industrial pure water, and a test filter for collecting specific cells from body fluids such as blood and saliva.
  • the test filter include a test filter for blood glucose level test, urine sugar test, lifestyle-related disease test, genetic test, tumor marker test, blood test, and the like.
  • the nonwoven fabric 10 can be manufactured by, for example, the nonwoven fabric manufacturing facility 20 shown in FIG.
  • the nonwoven fabric manufacturing facility 20 is for forming the fiber 11 and manufacturing the nonwoven fabric 10 using an electrospinning method.
  • the nonwoven fabric manufacturing facility 20 includes a solution preparation unit 21 and a nonwoven fabric manufacturing apparatus 22.
  • the details of the nonwoven fabric manufacturing apparatus 22 are shown in another drawing, and in FIG. 4, only a part of the nonwoven fabric manufacturing apparatus 22 is shown.
  • the solution preparation unit 21 is for preparing the solution 25 that forms the fiber 11.
  • the solution preparation unit 21 prepares the solution 25 by dissolving the cellulose polymer 15 as a fiber material to be the fiber 11 in the solvent 26.
  • the solution 25 is discharged from each of nozzles 27a to 27c described later, and forms the fiber 11 on the support 28.
  • nozzle 27a, the nozzle 27b, and the nozzle 27c are not distinguished, they are referred to as a nozzle 27.
  • V unit: ml / s, milliliter / second
  • the evaporation rate V and the average diameter DF of the fiber 11 formed on the support 28 are 1 ⁇ V / DF ⁇ 10 is satisfied. More preferably, 2 ⁇ V / DF ⁇ 9, and further preferably 3 ⁇ V / DF ⁇ 8.
  • V / DF is set to the above range by adjusting at least one of the evaporation rate V and the average diameter DF.
  • the evaporation rate V is obtained by the following equation (1).
  • C is the concentration of the solution 25 (unit:%).
  • the concentration C is obtained by a calculation formula of ⁇ M1 / (M1 + M2) ⁇ ⁇ 100, where the mass of the fiber material is M1 and the mass of the solvent is M2.
  • M1 is the mass of the cellulosic polymer 15
  • M2 is the mass of the solvent 26.
  • Q is the discharge amount of the solution 25 from the nozzle 27 (the volume discharged per hour, the unit is ml / h, milliliter / hour).
  • ⁇ 2 is the density of the solution 25 (unit: g / ml).
  • the evaporation rate V can be adjusted by increasing or decreasing at least one of the density C, the discharge amount Q, and the density ⁇ 2.
  • the evaporation rate V can also be adjusted by adjusting the formulation of the solvent 26 (for example, the component ratio when the solvent 26 is a mixture of a plurality of components).
  • the average diameter DF can be adjusted by increasing or decreasing at least one of the ejection amount Q, the concentration C, the applied voltage described later, and the distance L from the nozzle 27 to the support 28.
  • the temperature of the spinning space which is the space between the nozzle 27 and the support 28, is approximately 25 ° C., and therefore the evaporation rate V is obtained at 25 ° C., approximately the same as the temperature of the spinning space.
  • V ⁇ (1-0.01C) ⁇ Q ⁇ 10 ⁇ 3 ⁇ / (3600 ⁇ ⁇ 2) (1)
  • the solvent 26 may be composed of one kind of compound or may be composed of two or more kinds of compounds. However, since the solvent 26 has a function of adjusting the evaporation rate V in addition to the viewpoint of dissolving the fiber material, the solvent 26 is a mixture composed of two or more kinds of compounds from the viewpoint of adjusting the evaporation rate V. preferable.
  • the solvent 26 of this example is also a mixture and contains a plurality of compounds. For example, dichloromethane is used as the first compound 26a, and methanol is used as the second compound 26b. In addition to the first compound 26a and the second compound 26b, other compounds different from the first compound 26a and the second compound 26b are used as the third compound, the fourth compound,.
  • the solvent 26 may be configured as follows.
  • Solvent 26 preferably has a boiling point of 90 ° C. or lower.
  • the boiling point of the compound having the largest mass ratio is regarded as the boiling point of the solvent 26.
  • the solvent 26 is a mixture of three or more types of compounds and there are a plurality of compounds having the largest mass ratio, the boiling point of the compound having the highest boiling point is regarded as the boiling point of the solvent 26.
  • the solvent 26 is preferably an organic compound, that is, an organic solvent.
  • the solvent 26 is methanol, ethanol, isopropanol, butanol, benzyl alcohol, acetone, methyl ethyl ketone, cyclohexanone, methyl acetate, ethyl acetate, propyl acetate, butyl acetate, methyl formate, Ethyl formate, hexane, cyclohexane, dichloromethane, chloroform, carbon tetrachloride, benzene, toluene, xylene, dimethylformamide, N-methylpyrrolidone, diethyl ether, dioxane, tetrahydrofuran, 1-methoxy-2-propanol and the like can be used. These may be used singly or in combination of two or more.
  • methanol, dichloromethane, chloroform, toluene, acetone, tetrahydrofuran, or the like can be used as the solvent 26. These may also be used alone or in combination of two or more.
  • the moisture content of the fiber 11 on the support 28 is preferably 3.0% or more, that is, at least 3.0%.
  • the water content is more preferably in the range of 3.0% to 10.0%, and preferably in the range of 4.0% to 9.0%, and preferably 5.0% to 8.%. More preferably, it is in the range of 0% or less.
  • the nonwoven fabric manufacturing facility 20 includes pipes 33a to 33c that connect the solution preparation unit 21 and the nonwoven fabric manufacturing apparatus 22, and the nonwoven fabric manufacturing apparatus 22 has nozzles 27a to 27c arranged in a state of being separated from each other. .
  • the pipes 33a to 33c are for guiding the solution 25.
  • the pipe 33a connects the solution preparation unit 21 and the nozzle 27a
  • the pipe 33b connects the solution preparation unit 21 and the nozzle 27b
  • the pipe 33c connects the solution preparation unit 21 and the nozzle 27c.
  • the solution 25 is discharged from each of the nozzles 27a to 27c.
  • the solutions 25 exiting from the nozzles 27a to 27c form the fibers 11, respectively.
  • the pipe 33a, the pipe 33b, and the pipe 33c are not distinguished, they are described as the pipe 33.
  • a long support 28 is used to collect and deposit the fibers 11 (hereinafter collectively referred to as accumulation) and to support the nonwoven fabric 10, and the support 28 is moved in the longitudinal direction. ing.
  • the horizontal direction in FIG. 3 is the width direction of the support 28, and the depth direction in FIG. 3 is the moving direction of the support 28.
  • the nozzles 27a to 27c are arranged in this order in the width direction of the support 28.
  • the number of nozzles 27 is three, but the number of nozzles 27 is not limited to this.
  • Each of the pipes 33a to 33c is provided with a pump 38 for sending the solution 25 to the nozzle 27. By changing the number of rotations of the pump 38, each discharge amount of the solution 25 discharged from the nozzles 27a to 27c is adjusted.
  • the nozzles 27a to 27c are held by a holding member 41.
  • the holding member 41 and the nozzle 27 constitute a nozzle unit 42 of the nonwoven fabric manufacturing apparatus 22.
  • the nonwoven fabric manufacturing apparatus 22 will be described with reference to FIG. FIG. 4 shows a case when viewed from the nozzle 27 a side of FIG. 3, and for the nozzle 27, only the nozzle 27 a is illustrated.
  • the nonwoven fabric manufacturing apparatus 22 includes a chamber 45, the above-described nozzle unit 42, a stacking unit 50, a power source 51, and the like.
  • the chamber 45 accommodates, for example, the nozzle unit 42 and a part of the stacking unit 50.
  • the chamber 45 is configured to be hermetically sealed, thereby preventing the solvent gas from leaking to the outside.
  • the solvent gas is obtained by vaporizing the solvent 26 of the solution 25.
  • the chamber 45 includes a humidity adjusting mechanism 45a that adjusts the internal relative humidity (hereinafter simply referred to as humidity).
  • the humidity adjusting mechanism 45 a sends a gas (for example, air) whose humidity has been adjusted to the chamber 45, collects the atmosphere in the chamber 45, adjusts the humidity again, and sends it to the chamber 45. In this way, the humidity inside the chamber 45 is adjusted.
  • This humidity adjustment is performed to adjust the humidity of the spinning space described above. That is, the chamber 45 has a function of partitioning the spinning space from the external space and adjusting the humidity of the spinning space.
  • the adjustment of the humidity of the spinning space is not limited to the method of this example using the chamber 45.
  • the humidity of the spinning space may be adjusted by a chamber that defines the spinning space in the chamber 45.
  • the spinning space humidity is preferably 10% or more and 30% or less.
  • the humidity may change during the formation of the fiber 11 and the production of the nonwoven fabric 10 as long as it is within this range.
  • the humidity of the spinning space is more preferably in the range of 15% to 25%.
  • the nozzle unit 42 is disposed in the upper part of the chamber 45.
  • the tip from which the solution 25 of the nozzle 27 exits is directed to the collector 52 disposed below the nozzle 27 in FIG.
  • a tip opening an opening formed in the tip of the nozzle 27
  • a generally conical Taylor cone 53 is formed by the solution 25 in the tip opening.
  • the stacking unit 50 is disposed below the nozzle 27.
  • the stacking unit 50 includes a collector 52, a collector rotating unit 56, a support supply unit 57, and a support winding unit 58.
  • the collector 52 attracts the solution 25 from the nozzle 27 and collects the formed fiber 11 as the nonwoven fabric 10, and in this embodiment, collects it on a support 28 described later.
  • the collector 52 is composed of an endless belt formed in a ring shape with a metal strip.
  • the collector 52 may be made of a material that is charged when a voltage is applied by the power supply 51, and is made of, for example, stainless steel.
  • the collector rotating unit 56 includes a pair of rollers 61 and 62, a motor 60, and the like.
  • the collector 52 is stretched horizontally around the pair of rollers 61 and 62.
  • a motor 60 disposed outside the chamber 45 is connected to the shaft of one roller 61 and rotates the roller 61 at a predetermined speed. This rotation causes the collector 52 to move and circulate between the rollers 61 and 62.
  • the moving speed of the collector 52 is, for example, 0.2 m / min, but is not limited thereto.
  • the collector 52 is supplied with a support 28 made of, for example, an aluminum sheet by a support supply unit 57.
  • the support 28 is for collecting the fibers 11 and obtaining the nonwoven fabric 10.
  • the support body supply unit 57 has a delivery shaft 57a.
  • a support roll 63 is attached to the delivery shaft 57a.
  • the support roll 63 is configured by winding the support 28 around a winding core 64.
  • the support winding unit 58 has a winding shaft 67.
  • the winding shaft 67 is rotated by a motor (not shown), and the support body 28 on which the nonwoven fabric 10 is formed is wound around the core 68 to be set.
  • this nonwoven fabric manufacturing apparatus 22 has a function of forming the fiber 11 and a function of forming the nonwoven fabric 10.
  • the support 28 may be placed on the collector 52 and moved by moving the collector 52.
  • the nonwoven fabric 10 may be formed by directly collecting the fibers 11 on the collector 52. However, depending on the material forming the collector 52 or the surface state of the collector 52, the nonwoven fabric 10 is stuck and is difficult to peel off. There is a case. For this reason, it is preferable to guide the support body 28 on which the nonwoven fabric 10 is difficult to adhere to the collector 52 as in this embodiment, and to integrate the fiber 11 on the support body 28.
  • the power supply 51 applies a voltage to the nozzle 27 and the collector 52, thereby charging the nozzle 27 to the first polarity and charging the collector 52 to the second polarity opposite to the first polarity. Part.
  • the solution 25 is charged and exits the nozzle 27 in a charged state.
  • the holding member 41 and the nozzle 27 are electrically connected, and the voltage is applied to the nozzle 27 via the holding member 41 by connecting the power source 51 to the holding member 41.
  • the method of applying the voltage is not limited to this.
  • a voltage may be applied to each nozzle 27 by connecting a power source 51 to each nozzle 27.
  • the nozzle 27 is charged positively (+) and the collector 52 is negatively charged ( ⁇ ).
  • the polarity of the nozzle 27 and the collector 52 may be reversed.
  • the collector 52 side may be grounded and the potential may be set to zero. Due to the charging, the solution 25 is ejected from the Taylor cone 53 toward the collector 52 as a spinning jet 69.
  • the solution 25 is charged by applying a voltage to the nozzle 27, but the solution 25 may be charged in the pipe 33 and the charged solution 2 may be guided to the nozzle 27.
  • the distance L between the nozzle 27 and the collector 52 varies depending on the type of the cellulosic polymer 15 and the solvent 26, the mass ratio of the solvent 26 in the solution 25, and the like, but is preferably in the range of 30 mm or more and 500 mm or less. For example, it is 150 mm.
  • the voltage (applied voltage) applied to the nozzle 27 and the collector 52 is preferably 5 kV or more and 200 kV or less. From the viewpoint of forming the fiber 11 thinner, the applied voltage is preferably as high as possible within this range. In this embodiment, it is 40 kV, for example.
  • a voltage is applied by the power source 51 to the nozzle 27 and the collector 52 that circulates and moves.
  • the nozzle 27 is positively charged as the first polarity
  • the collector 52 is negatively charged as the second polarity.
  • the solution 25 is continuously supplied from the solution preparation unit 21 to the nozzle 27, and the support 28 is continuously supplied onto the moving collector 52.
  • the solution 25 is charged positively as the first polarity by passing through each of the nozzles 27a to 27c, and exits from the tip openings of the nozzles 27a to 27c in a charged state.
  • the collector 52 attracts the solution 25 that has exited from the tip opening while being charged to the first polarity.
  • a Taylor cone 53 is formed at the tip opening, and the spinning jet 69 exits from the Taylor cone 53 toward the collector 52.
  • the spinning jet 69 charged to the first polarity splits into a smaller diameter due to repulsion due to its own charge and / or extends to a smaller diameter while drawing a spiral trajectory while heading toward the collector 52.
  • the fiber 11 is collected on the support 28. Since the fiber 11 is deposited in a very short time, it is collected as the nonwoven fabric 10.
  • the thickness of the nonwoven fabric 10 can be adjusted by increasing / decreasing the deposition amount. For example, the amount of deposition can be increased or decreased by adjusting the moving speed of the support 28.
  • the fiber 11 having an average diameter DF of 0.10 ⁇ m or more and 5.00 ⁇ m or less is formed, the porosity is 90% or more, and the average pore diameter DA is 0.5 ⁇ m or more.
  • the non-woven fabric 10 having a pore diameter standard deviation of 1.5 ⁇ m or less is obtained within a range of 50 ⁇ m or less. Specifically, by satisfying 1 ⁇ V / DF, the spinning jet 69 becomes thinner than in the case of V / DF ⁇ 1, so that the solvent 26 is sufficiently evaporated and the average diameter DF is within the above range. It becomes the fiber 11 and reaches the support 28.
  • the fibers 11 are deposited on the support 28 in a non-adhered state with each other or in a state in which the adhesive force is extremely small even when bonded.
  • the nonwoven fabric 10 has a porosity of 90% or more, an average pore diameter DA in the range of 0.5 ⁇ m to 50 ⁇ m, and a standard deviation of the pore diameter of 1.5 ⁇ m or less.
  • V / DF ⁇ 10 the spinning jet 69 reliably forms the fiber 11 and does not become beads (microspheres) as compared with the case of 10 ⁇ V / DF. Since the beads are not formed, the beads do not fill the gap 13 of the nonwoven fabric 10 on the support 28. As a result, the porosity is surely 90% or more.
  • the spinning space is adjusted to a humidity of 10% or more and 30% or less, the moisture content of the fiber 11 on the support 28 is surely 3.0% or more, and does not exceed 10%. Since the moisture content of the fiber 11 on the support 28 is 3.0% or more, the spinning jet 69 generated thereafter is more reliably formed as the fiber 28 as compared with the case where it is less than 3.0%. Accumulate and deposit on top. This serves as an earth function for releasing electric charges due to moisture contained in the fiber 11 collected on the support 37, and therefore, the spinning jet 69 generated in the spinning space is suppressed from scattering to the periphery. In this state, it is considered that the fiber 11 is reached toward the support 28.
  • the nonwoven fabric 10 is more reliably manufactured with a porosity of 90% or more.
  • the moisture content is 10% or less, compared to the case where the moisture content is larger than 10%, the fiber 11 that has absorbed moisture is prevented from being deformed by its own weight, and the gap is easily maintained high.
  • the solvent 26 having a boiling point of 90 ° C. or lower By using the solvent 26 having a boiling point of 90 ° C. or lower, the solvent 26 is more easily evaporated from the spinning jet 69 and excessive evaporation is suppressed as compared with the case where the solvent 26 having a boiling point higher than 90 ° C. is used.
  • the spinning jet 69 evaporates an appropriate amount of the solvent 26 while passing through the spinning space in which the humidity is adjusted, as compared with the case where water is used, for example. And keep the balance of spinning space and moisture. As a result, it is easy to balance the degree of drying of the fiber 11 and the moisture content.
  • the fiber 11 forms the fluffy nonwoven fabric 10 and is sent to the support winding portion 58 together with the support 28.
  • the nonwoven fabric 10 is wound around the core 68 in a state where it overlaps the support 28. After the winding core 68 is removed from the winding shaft 67, the nonwoven fabric 10 is separated from the support 28.
  • the nonwoven fabric 10 thus obtained is long, but after that, for example, it may be cut into a desired size.
  • a circulating belt is used as the collector 52, but the collector is not limited to a belt.
  • the collector may be a fixed flat plate or a cylindrical rotating body.
  • the support 28 it is preferable to use the support 28 so that the nonwoven fabric 10 can be easily separated from the collector.
  • a rotating body a cylindrical sheet material made of fibers is formed on the peripheral surface of the rotating body. Therefore, after spinning, the cylindrical sheet material is extracted from the rotating body, and is formed into a desired size and shape. Cut it out.
  • the nozzle 27 is disposed with the tip opening facing downward, and the collector 52 is disposed under the nozzle 27, whereby the solution 25 is discharged downward.
  • the discharge direction of the solution 25 is not limited to this example.
  • the solution 25 may be discharged upward by disposing the nozzle 27 with the tip opening facing upward and disposing the collector 52 on the nozzle 27.
  • Example 1 to [Example 8] Using the nonwoven fabric manufacturing facility 20, the nonwoven fabric 10 was manufactured under the conditions shown in Table 1, and Examples 1 to 8 were obtained. The thickness of the manufactured nonwoven fabric 10 is 4000 micrometers as above-mentioned. The fiber material used is described in the “fiber material” column of Table 1.
  • the solvent 26 was a mixture of the first compound 26a and the second compound 26b.
  • the first compound 26a and the second compound 26b used are shown in Table 1.
  • Table 1 “DMC” is dichloromethane, “MeOH” is methanol, and “NMP” is N-methylpyrrolidone.
  • “Moisture content” in Table 1 is the moisture content of the fiber 11 integrated on the support 28. In the column “Standard deviation of pore diameter” in Table 1, when the result of rounding off the value obtained with two decimal places is 0.0, “ ⁇ 0.1” is entered.
  • the fluffiness which is the elasticity when the obtained nonwoven fabric 10 is repeatedly pressed with two fingers, corresponds to the following compression rate evaluation. Specifically, the compression ratio was higher as more fluffy feeling was felt. Therefore, the compression ratio was evaluated as an evaluation of fluffiness.
  • the compression rate was evaluated by the following method. First, a size of 10 cm ⁇ 10 cm was cut out from the nonwoven fabric 10 as a sample. The sample was allowed to stand with the first surface 10A facing upward, a weight of 800 g was placed on the first surface 10A, and the thickness of the loaded sample was measured with calipers. In any sample, when the weight was removed, the first surface 10A returned to the original height, and the shape was restored. The compression ratio was obtained by dividing the thickness before loading the weight (4000 ⁇ m) by the thickness of the loaded state. The compression ratio is shown in Table 1.

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  • Engineering & Computer Science (AREA)
  • Textile Engineering (AREA)
  • Mechanical Engineering (AREA)
  • Chemical & Material Sciences (AREA)
  • Dispersion Chemistry (AREA)
  • Nonwoven Fabrics (AREA)
  • Artificial Filaments (AREA)
  • Spinning Methods And Devices For Manufacturing Artificial Fibers (AREA)

Abstract

Provided are a nonwoven fabric having a cushioning feel, a method for forming a fiber, and a method for manufacturing the nonwoven fabric. According to the present invention, nonwoven fabric manufacturing equipment (20) forms a fiber (11) from a solution (25) and manufactures a nonwoven fabric. The nonwoven fabric (10) is formed of a fiber (11). The nonwoven fabric (10) has pores (13) formed therein. The average diameter DF of the fiber 11 is within the range of 0.10 μm to 5.00 μm inclusive. The nonwoven fabric (10) has a porosity of at least 90%. The average pore diameter is within the range of 0.5 μm to 50 μm inclusive, and the standard deviation of the pore diameter is at most 1.5 μm.

Description

不織布、ファイバ形成方法及び不織布製造方法Nonwoven fabric, fiber forming method and nonwoven fabric manufacturing method

 本発明は、不織布、ファイバ形成方法及び不織布製造方法に関する。 The present invention relates to a nonwoven fabric, a fiber forming method, and a nonwoven fabric manufacturing method.

 ファイバで形成されている不織布が知られている。ファイバとしては、例えば数nm以上1000nm未満のナノオーダの径を有するいわゆるナノファイバ、及び、数μm以上1000μm未満のマイクロメートルオーダの径を有するいわゆるミクロンファイバがある。 Nonwoven fabrics made of fiber are known. Examples of the fiber include a so-called nanofiber having a nano-order diameter of several nm or more and less than 1000 nm, and a so-called micron fiber having a diameter of several micrometers or more and less than 1000 μm.

 こうした不織布などの繊維からなる層(以下、繊維層と称する)を備える繊維構造体として、例えば特許文献1には、バッテリーなどにおけるセパレータ、または絶縁材として用いられ、平均直径が50nm~3000nmの高分子繊維からなる繊維層を備える繊維構造体が記載されている。この繊維構造体は、所定の方法により測定した面圧5MPaにおける最大圧縮率が20%以上とされている。繊維層は、平均孔径が0.01~15μm、厚みが0.0025~0.3mm、多孔度が20~90%、秤量が1~90g/m、フラジール通気度が46m/分/m未満、マクミラン数が2~15とされている。 As a fiber structure including a layer made of fibers such as nonwoven fabric (hereinafter referred to as a fiber layer), for example, in Patent Document 1, it is used as a separator or an insulating material in a battery or the like, and has a high average diameter of 50 nm to 3000 nm. A fiber structure comprising a fiber layer made of molecular fibers is described. This fiber structure has a maximum compression rate of 20% or more at a surface pressure of 5 MPa measured by a predetermined method. The fiber layer has an average pore diameter of 0.01 to 15 μm, a thickness of 0.0025 to 0.3 mm, a porosity of 20 to 90%, a weighing of 1 to 90 g / m 2 , and a fragile air permeability of 46 m 3 / min / m. It is less than 2 and the Macmillan number is 2-15.

 ところで、ナノファイバなどのファイバ、及び、こうしたファイバで形成されている不織布を製造する方法として、電界紡糸法が知られている。電界紡糸法は、特許文献1に記載されるように、エレクトロスピニング法などとも呼ばれ、例えばノズルとコレクタと電源とを有する電界紡糸装置(エレクトロスピニング装置とも呼ばれる)を用いて行われる。一般的な電界紡糸装置では、電源によりノズルとコレクタとの間に電圧を印加し、例えば、ノズルをマイナス、コレクタをプラスに帯電させる。 Incidentally, an electrospinning method is known as a method for producing a fiber such as a nanofiber and a non-woven fabric formed of such a fiber. As described in Patent Document 1, the electrospinning method is also referred to as an electrospinning method or the like, and is performed using, for example, an electrospinning device (also referred to as an electrospinning device) having a nozzle, a collector, and a power source. In a general electrospinning apparatus, a voltage is applied between a nozzle and a collector by a power source, and for example, the nozzle is negatively charged and the collector is positively charged.

 電圧を印加した状態でノズルから原料である溶液を出した場合には、ノズルの先端の開口にテイラーコーンと呼ばれる溶液で構成される円錐状の突起が形成される。印加電圧を徐々に増加し、クーロン力が溶液の表面張力を上回ると、テイラーコーンの先端から溶液が飛び出し、紡糸ジェットが形成される。紡糸ジェットはクーロン力によってコレクタまで移動し、コレクタ上でファイバとして捕集され、コレクタ上にはファイバで構成された不織布が形成される。 When a solution, which is a raw material, is taken out from the nozzle in a state where a voltage is applied, a conical projection composed of a solution called a Taylor cone is formed at the opening at the tip of the nozzle. When the applied voltage is gradually increased and the Coulomb force exceeds the surface tension of the solution, the solution is ejected from the tip of the Taylor cone and a spinning jet is formed. The spinning jet moves to the collector by the Coulomb force and is collected as a fiber on the collector, and a nonwoven fabric composed of the fiber is formed on the collector.

国際公開第2014/010753号International Publication No. 2014/010753

 ナノファイバ及びミクロンファイバで形成されている不織布は、種々の分野における用途開発が盛んに行われている。期待される用途には例えば断熱材、吸音材、フィルタなどが挙げられ、また、医療用不織布としての利用も期待される。 Nonwoven fabrics made of nanofibers and micronfibers have been actively developed in various fields. Expected uses include, for example, a heat insulating material, a sound absorbing material, a filter, and the like, and are expected to be used as a medical nonwoven fabric.

 しかしながら、特許文献1に記載される繊維構造体及び繊維層は、セパレータへの利用を前提としていることから、電解質を良好に吸収するための繊維層の多孔度、アノード及びカソード間でイオンが流れやすくするための厚み、アノード及びカソード間のデンドライドショートなどを防止するための秤量などを特定している。そのため、例えば吸音材及び断熱材としては吸音性能及び断熱性能が不足する等、上記のような用途への展開は難しい。この点、ふわふわ(fluffy)感が有る不織布、すなわち空気を多量に包み、かつ、柔らかな不織布であれば、吸音性能、断熱性能などをもち、用途の広がりが期待できる。 However, since the fiber structure and the fiber layer described in Patent Document 1 are premised on use in a separator, the porosity of the fiber layer for favorably absorbing the electrolyte, ions flow between the anode and the cathode. The thickness for facilitating the measurement and the weighing for preventing the dendride short between the anode and the cathode are specified. Therefore, for example, the sound absorbing material and the heat insulating material are difficult to develop in the above-mentioned applications such as insufficient sound absorbing performance and heat insulating performance. In this respect, a non-woven fabric having a fluffy feeling, that is, a soft non-woven fabric that wraps a large amount of air, has sound absorption performance, heat insulation performance, and the like, and can be expected to expand its application.

 そこで、本発明は、ふわふわ感がある不織布と、その不織布を得るファイバ形成方法および不織布製造方法とを提供することを目的とする。 Therefore, an object of the present invention is to provide a nonwoven fabric having a fluffy feeling, a fiber forming method for obtaining the nonwoven fabric, and a nonwoven fabric manufacturing method.

 本発明の不織布は、平均径が0.10μm以上5.0μm以下の範囲内であるファイバを備え、空隙率が少なくとも90%であり、平均孔径が0.5μm以上50μm以下の範囲内であり、かつ、孔径の標準偏差が大きくても1.5μmである。 The nonwoven fabric of the present invention comprises a fiber having an average diameter in the range of 0.10 μm to 5.0 μm, a porosity of at least 90%, and an average pore diameter in the range of 0.5 μm to 50 μm, And even if the standard deviation of a hole diameter is large, it is 1.5 micrometers.

 ファイバは、セルロース系ポリマーで形成されていることが好ましい。 The fiber is preferably formed of a cellulosic polymer.

 本発明のファイバ形成方法は、溶媒にファイバ材が溶解している溶液とコレクタとの間に電圧を印加し、上記溶液をノズルからコレクタへ噴出することによりファイバを形成する。溶媒の蒸発速度をVμl/sとし、ファイバの平均径をDFμmとするときに、1≦V/DF≦10である。 In the fiber forming method of the present invention, a fiber is formed by applying a voltage between a solution in which a fiber material is dissolved in a solvent and the collector, and ejecting the solution from the nozzle to the collector. When the evaporation rate of the solvent is V μl / s and the average diameter of the fiber is DF μm, 1 ≦ V / DF ≦ 10.

 ファイバの含水率を少なくとも3.0%にすることが好ましい。 It is preferable that the moisture content of the fiber is at least 3.0%.

 ノズルとコレクタとの間の紡糸空間の相対湿度を10%以上30%以下にすることにより、ファイバの含水率を調整することが好ましい。紡糸空間は、内部の相対湿度を調整する湿度調整機構を備えるチャンバにより、外部空間と仕切られていることが好ましい。 It is preferable to adjust the moisture content of the fiber by setting the relative humidity of the spinning space between the nozzle and the collector to 10% to 30%. The spinning space is preferably partitioned from the external space by a chamber having a humidity adjusting mechanism for adjusting the internal relative humidity.

 ファイバ材は、セルロース系ポリマーであることが好ましい。セルロース系ポリマーは、セルロースアシレートであることが好ましい。セルロースアシレートは、セルロースアセテートプロピオネートと、セルローストリアセテートとのいずれかであることが好ましい。 The fiber material is preferably a cellulosic polymer. The cellulosic polymer is preferably cellulose acylate. The cellulose acylate is preferably either cellulose acetate propionate or cellulose triacetate.

 溶媒は、複数の化合物の混合物であることが好ましい。溶媒は、ジクロロメタンとメタノールとを含有することが好ましい。 The solvent is preferably a mixture of a plurality of compounds. The solvent preferably contains dichloromethane and methanol.

 本発明の不織布製造方法は、溶媒にファイバ材が溶解している溶液とコレクタとの間に電圧を印加し、上記溶液をノズルから噴出することにより形成したファイバを、コレクタ上に不織布として捕集する。溶媒の蒸発速度をVμl/sとし、ファイバの平均径をDFμmとするときに、1≦V/DF≦10である。 The non-woven fabric production method of the present invention collects fibers formed by applying a voltage between a solution in which a fiber material is dissolved in a solvent and a collector and ejecting the solution from a nozzle as a non-woven fabric on the collector. To do. When the evaporation rate of the solvent is V μl / s and the average diameter of the fiber is DF μm, 1 ≦ V / DF ≦ 10.

 本発明によると、ふわふわ感がある不織布が得られる。 According to the present invention, a nonwoven fabric with a fluffy feeling can be obtained.

一実施形態である不織布の一部の概略斜視図である。It is a schematic perspective view of a part of the nonwoven fabric which is one Embodiment. 孔径分布及び標準偏差の説明図である。It is explanatory drawing of a hole diameter distribution and a standard deviation. 不織布製造設備の概略図である。It is the schematic of a nonwoven fabric manufacturing equipment. 不織布製造設備の概略図である。It is the schematic of a nonwoven fabric manufacturing equipment.

 図1に示す本実施形態の不織布10は、ファイバ11で形成されている。不織布10には、ファイバ11によって画定された空間領域としての空隙13が、空気が存在する部分として複数形成されている。このように、不織布10は、内部に空気を含んでいる。なお、図1には、図の煩雑化を避けるために、不織布10の厚み方向Zにおいて一方の表面(以下、第1表面と称する)10A側の一部のみを描いてある。したがって、不織布10は、ファイバ11が厚み方向Zにおける図1の下側に、さらに多数重なった構造となっている。 The nonwoven fabric 10 of this embodiment shown in FIG. In the nonwoven fabric 10, a plurality of voids 13 as space regions defined by the fibers 11 are formed as portions where air exists. Thus, the nonwoven fabric 10 contains air inside. In FIG. 1, only a part of one surface (hereinafter referred to as a first surface) 10 </ b> A side in the thickness direction Z of the nonwoven fabric 10 is drawn in order to avoid complication of the drawing. Therefore, the nonwoven fabric 10 has a structure in which a large number of fibers 11 are further stacked on the lower side in FIG.

 複数の空隙13は、不織布10の厚み方向Zにおいて連通している場合には、不織布10の厚み方向Zに貫通した空孔を形成する。この空孔は、不織布10を例えばフィルタに利用した場合には、フィルタの孔として機能する。また、空隙13の中には、空孔を形成せずに、厚み方向Zで非貫通、例えばファイバ11によって閉じられた空間領域として存在しているものもある。 When the plurality of voids 13 communicate with each other in the thickness direction Z of the nonwoven fabric 10, holes that penetrate in the thickness direction Z of the nonwoven fabric 10 are formed. The holes function as filter holes when the nonwoven fabric 10 is used for a filter, for example. In addition, some of the gaps 13 exist as a space region that does not penetrate in the thickness direction Z, for example, is closed by the fiber 11 without forming holes.

 不織布10は、ファイバ11を含んでいればよく、ファイバ11に加えて、素材が異なる他のファイバを備えてもよい。図1では、第1表面10AをXY平面に沿った状態に描いており、XY平面に直交するZを不織布10の厚み方向としている。 The nonwoven fabric 10 only needs to include the fiber 11, and may include other fibers having different materials in addition to the fiber 11. In FIG. 1, the first surface 10 </ b> A is drawn along the XY plane, and Z perpendicular to the XY plane is the thickness direction of the nonwoven fabric 10.

 ファイバ11は、径D1が概ね一定に形成されている。径D1の平均値(以下、平均径と称する)DF(単位はμm)は、0.10μm以上5.00μm以下の範囲内であることが好ましい。平均径DFが0.10μm以上であることにより、0.10μm未満の場合と比べて、ファイバ片の脱離が抑制される。ファイバ片の脱離の抑制とは、不織布10からのファイバ片の脱離が抑制されることを意味し、ファイバ片の脱離が抑制されていることは不織布10としての優れた耐久性につながる。平均径DFが5.00μm以下であることにより、5.00μmよりも大きい場合に比べて、不織布10は、含んでいる空気の体積割合(以下、空隙率と称する)が同じであっても、より柔らかくなる。また、平均径DFが5.00μm以下であることにより、5.00μmよりも大きい場合に比べて、不織布10は柔らかさが同程度であっても、空隙率がより大きくなり、その結果、吸音材、断熱材として用いた場合の吸音性能、断熱性能が高くなり、また、フィルタに利用した場合のろ過処理量が高くなる。径は、0.15μm以上4.00μm以下の範囲内であることがより好ましく、0.20μm以上3.00μm以下の範囲内であることがさらに好ましい。 The fiber 11 is formed with a substantially constant diameter D1. The average value of diameter D1 (hereinafter referred to as average diameter) DF (unit: μm) is preferably in the range of 0.10 μm or more and 5.00 μm or less. When the average diameter DF is 0.10 μm or more, detachment of the fiber piece is suppressed as compared with the case where the average diameter DF is less than 0.10 μm. The suppression of the fiber piece detachment means that the fiber piece detachment from the nonwoven fabric 10 is suppressed, and the suppression of the fiber piece detachment leads to excellent durability as the nonwoven fabric 10. . Since the average diameter DF is 5.00 μm or less, the nonwoven fabric 10 has the same volume ratio of air (hereinafter referred to as porosity) compared to the case where the average diameter DF is larger than 5.00 μm. It becomes softer. Further, when the average diameter DF is 5.00 μm or less, the non-woven fabric 10 has a higher porosity even if the nonwoven fabric 10 has the same degree of softness as compared with the case where the average diameter DF is larger than 5.00 μm. When used as a material or a heat insulating material, the sound absorbing performance and the heat insulating performance are increased, and the amount of filtration treatment when used for a filter is increased. The diameter is more preferably in the range of 0.15 μm to 4.00 μm, and still more preferably in the range of 0.20 μm to 3.00 μm.

 平均径DFは、走査型電子顕微鏡で撮影した画像から100本のファイバ11の径を測定し、平均値を算出することにより求めることができる。 The average diameter DF can be obtained by measuring the diameter of 100 fibers 11 from an image taken with a scanning electron microscope and calculating the average value.

 不織布10は、空隙率が90%以上、すなわち、少なくとも90%である。このように空隙率が非常に高い不織布10は、ふわふわ感(fluffy)がある。すなわち、内部に空気を多量に含んでおり、かつ柔らかい。このように空気を多量に含んでいるから、90%未満の空隙率である場合に比べて、用途に広がりをもつ。例えば、90%未満の空隙率である場合に比べて優れた吸音性能及び断熱性能を示すから、吸音材及び断熱材として利用できる。また、90%未満の空隙率である場合に比べて、フィルタにした場合には大きなろ過処理性能を示す。ろ過処理性能とは、単位時間あたりの処理量、及び/または、目詰まりが抑制された状態の持続性などを意味する。なお、フィルタに用いる場合には、不織布10を加熱することにより、ファイバ11同士を接着した上で、フィルタとして用いることがより好ましい場合がある。空隙率は99.8%以下であることが、不織布10としてのより高い耐久性が確保されるから好ましい。空隙率は、より好ましくは90%以上99.8%以下の範囲内であり、さらに好ましくは95%以上99.6%以下の範囲内であり、特に好ましくは97%以上99.4%以下の範囲内である。 The nonwoven fabric 10 has a porosity of 90% or more, that is, at least 90%. Thus, the nonwoven fabric 10 with a very high porosity has a fluffy feeling. That is, it contains a large amount of air inside and is soft. Since it contains a large amount of air in this way, it has a wider range of uses than when it has a porosity of less than 90%. For example, since the sound absorption performance and heat insulation performance superior to the case of a porosity of less than 90% are exhibited, it can be used as a sound absorption material and a heat insulation material. Moreover, compared with the case where it is the porosity of less than 90%, when it is set as a filter, a big filtration processing performance is shown. The filtration performance means the treatment amount per unit time and / or the sustainability of a state where clogging is suppressed. In addition, when using for a filter, after bonding the fibers 11 by heating the nonwoven fabric 10, using as a filter may be more preferable. The porosity is preferably 99.8% or less because higher durability as the nonwoven fabric 10 is secured. The porosity is more preferably in the range of 90% or more and 99.8% or less, further preferably in the range of 95% or more and 99.6% or less, and particularly preferably 97% or more and 99.4% or less. Within range.

 空隙率(単位は%)は、不織布10の秤量をW(単位はg/m)とし、厚みをH(単位はmm)とし、ファイバ11の比重をρ1(単位はkg/m)とするときに、[1-{(W/1000)/(H/1000)}/ρ1]×100で求めることができる。秤量Wは、不織布10を5cm×5cmに切り出し、質量を電子天秤(メトラー・トレド株式会社製)で測定し、その測定値を1mあたりに換算した値を用いる。厚みHは、本例では、非接触レーザー変位計(キーエンス株式会社製LK-H025)で測定している。 The porosity (unit:%) is W (unit: g / m 2 ), the thickness is H (unit: mm), and the specific gravity of the fiber 11 is ρ1 (unit: kg / m 3 ). Then, [1-{(W / 1000) / (H / 1000)} / ρ1] × 100 can be obtained. For the weighing W, the nonwoven fabric 10 is cut into 5 cm × 5 cm, the mass is measured with an electronic balance (manufactured by METTLER TOLEDO), and a value obtained by converting the measured value per 1 m 2 is used. In this example, the thickness H is measured by a non-contact laser displacement meter (LK-H025 manufactured by Keyence Corporation).

 ファイバ11同士は絡み合っており、厚み方向Zで重なる部分、及び/または、不織布10の面方向(XY平面内)において接している部分が接着していない(非接着である)ことが好ましく、本例でもそのようにしている。ただし、接着している箇所が部分的にあってもよく、接着している場合でもその接着力はごく弱い力で容易に剥がすことができる程度に小さく抑えてある。このように、ファイバ11同士は、絡み合っている状態、または接着していても接着力が小さく抑えられているから、空気を多量に含んだ状態で柔らかく、変形自在であり、そのため、例えば断熱材及び吸音材として用いる場合に施工場所の自由度が大きい。また、ファイバ11同士は、絡み合っている状態、または接着していても接着力が小さく抑えられているから、ファイバ11を例えば0.10μm以上5.00μm以下という小さな径にしている場合には、局部的に張力を付与することにより裂くこともできる。そのため、作業性にも優れる。 The fibers 11 are intertwined, and it is preferable that a portion overlapping in the thickness direction Z and / or a portion contacting in the surface direction (in the XY plane) of the nonwoven fabric 10 is not bonded (not bonded). This is the case in the example. However, there may be a part where the bonding is performed, and even when the bonding is performed, the bonding force is kept small enough to be easily peeled off by a very weak force. As described above, the fibers 11 are intertwined with each other, or even if they are bonded, the adhesive force is suppressed to be small. Therefore, the fibers 11 are soft and deformable in a state of containing a large amount of air. And when used as a sound-absorbing material, the degree of freedom of construction site is large. Further, since the fibers 11 are in an intertwined state, or the adhesive force is kept small even if they are bonded, when the fiber 11 has a small diameter of, for example, 0.10 μm or more and 5.00 μm or less, It can also be torn by applying tension locally. Therefore, it is excellent in workability.

 不織布10の厚みは、特に限定されず、後述のようにファイバ11の堆積量によって調整することができ、取り扱い場面及び/または用途等に応じて適宜設定してよい。例えば、取り扱い場面における作業性及び耐久性などの取り扱い性(ハンドリング)の観点では、例えば、100μm以上100000μm以下の範囲内であることが好ましい。また、吸音材または断熱材として用いる場合には、そのまま1枚で施工するために厚め(例えば2000μm以上100000μm以下の範囲内など)にしてもよいし、重ねた状態で施工するために薄め(例えば200μm以上1000μm以下の範囲内など)にしてもよい。なお、本例では、4000μmとしている。不織布10は、上記のように厚みに大きな自由度がありながらも、多量の空気を含んでおり、柔らかいため、用途が広い。 The thickness of the nonwoven fabric 10 is not particularly limited, and can be adjusted according to the amount of fiber 11 deposited as described later, and may be set as appropriate according to the handling situation and / or application. For example, from the viewpoint of handleability (handling) such as workability and durability in handling scenes, it is preferably in the range of 100 μm to 100,000 μm, for example. Further, when used as a sound absorbing material or a heat insulating material, it may be thickened (for example, within a range of 2000 μm or more and 100,000 μm or less) to be applied as it is, or thinned (for example, to be applied in a stacked state) It may be within a range of 200 μm or more and 1000 μm or less. In this example, it is 4000 μm. Although the nonwoven fabric 10 has a large degree of freedom in thickness as described above, it contains a large amount of air and is soft, and therefore has a wide range of uses.

 ここで、複数の空隙13が形成されている不織布10の平均孔径をDA(単位はμm)とする。平均孔径DAは0.5μm以上50μm以下の範囲内であり、かつ、孔径の標準偏差は1.5μm以下、すなわち大きくても1.5μmである。このように、孔径が、均一で、かつ、前述のように高い空隙率をもつから、例えばフィルタとして用いる場合には、高精度のろ過が効率よく実施される。平均孔径DAは、2μm以上30μm以下の範囲内がより好ましく、4μm以上20μm以下の範囲内がさらに好ましい。孔径の標準偏差は、1.0μm以下であることがより好ましく、0.5μm以下であることがさらに好ましく、このように小さく抑えられているほど好ましい。 Here, the average pore diameter of the nonwoven fabric 10 in which a plurality of voids 13 are formed is DA (unit: μm). The average pore diameter DA is in the range of 0.5 μm to 50 μm, and the standard deviation of the pore diameter is 1.5 μm or less, that is, 1.5 μm at most. Thus, since the pore diameter is uniform and has a high porosity as described above, for example, when used as a filter, highly accurate filtration is efficiently performed. The average pore diameter DA is more preferably in the range of 2 μm to 30 μm, and still more preferably in the range of 4 μm to 20 μm. The standard deviation of the pore diameter is more preferably 1.0 μm or less, further preferably 0.5 μm or less, and it is more preferable that the pore size is kept small.

 平均孔径DAは、以下の方法で求めることができる。まず、ファイバシート10から5cm角(5cm×5cm)に切り出し、サンプルとする。このサンプルを、表面張力が15.3mN/mのGALWICK(POROUS MATERIAL社製)に浸漬した後、パームポロメーター(POROUS MATERIAL社製)を用いて、バブルポイント法で測定することにより平均孔径DAは得られる。 The average pore diameter DA can be obtained by the following method. First, a 5 cm square (5 cm × 5 cm) is cut out from the fiber sheet 10 to obtain a sample. After immersing this sample in GALWICK (manufactured by POROUS MATERIAL) having a surface tension of 15.3 mN / m, the average pore diameter DA is determined by measuring by a bubble point method using a palm porometer (manufactured by POROUS MATERIAL). can get.

 孔径の標準偏差は、パームポロメーターが出力した孔径分布(孔径とその孔径をもつ空孔の存在量との相関関係データ)を用いて、以下の方法で求められる。まず、パームポロメーターにより出力された孔径分布(図2の実線で示す曲線L1であり、対応する縦軸は図2における左側縦軸である)において、全空孔の存在量を100%とする。これを、存在総量100%と称する。図3の破線で示す曲線L2(対応する縦軸は図2における右側縦軸である。)に示すように、孔径の大きい方から小さい方へ向かって空孔の存在量を積算していき、孔径の大きい方から存在総量が16%になる空孔の孔径をD(16%)とし、存在総量が84%になる空孔の孔径をD(84%)とする。そして、孔径の標準偏差は、{D(16%)-D(84%)}/2で算出する。 The standard deviation of the hole diameter is obtained by the following method using the hole diameter distribution (correlation data between the hole diameter and the abundance of holes having the hole diameter) output from the palm porometer. First, in the pore diameter distribution (curve L1 shown by the solid line in FIG. 2 and the corresponding vertical axis is the left vertical axis in FIG. 2) output by the palm porometer, the total amount of holes is 100%. . This is referred to as a total amount of 100%. As indicated by a curve L2 indicated by a broken line in FIG. 3 (the corresponding vertical axis is the right vertical axis in FIG. 2), the abundance of holes is accumulated from the larger hole diameter toward the smaller one, The hole diameter of the holes where the total existing amount is 16% from the larger hole diameter is D (16%), and the hole diameter of the holes whose existing total amount is 84% is D (84%). The standard deviation of the pore diameter is calculated by {D (16%) − D (84%)} / 2.

 ファイバ11は、樹脂(ポリマー)で形成されている。ポリマーとしては、溶媒に溶解することにより溶液にできるポリマーを用いている。ポリマーは、有機溶媒に溶解することにより溶液にできるポリマーであることが好ましい。例えば、ポリメチルメタクリレート(以下、PMMAと称する)、セルロース系ポリマー、ポリエステル、ポリウレタン、エラストマなどが挙げられる。本例では、例えば、セルロース系ポリマー15(図3参照)を用いている。 The fiber 11 is made of resin (polymer). As the polymer, a polymer that can be made into a solution by dissolving in a solvent is used. The polymer is preferably a polymer that can be made into a solution by dissolving in an organic solvent. Examples thereof include polymethyl methacrylate (hereinafter referred to as PMMA), cellulosic polymer, polyester, polyurethane, and elastomer. In this example, for example, a cellulose polymer 15 (see FIG. 3) is used.

 セルロース系ポリマー15はセルロースアシレートであることが好ましい。セルロースアシレートは、セルロースのヒドロキシ基を構成する水素原子の一部または全部がアシル基で置換されているセルロースエステルである。セルロースアシレートは、セルロースアセテートプロピオネート(以下、CAPと称する)と、セルローストリアセテート(以下、TACと称する)とのいずれかひとつであることが好ましい。 The cellulose polymer 15 is preferably cellulose acylate. Cellulose acylate is a cellulose ester in which some or all of the hydrogen atoms constituting the hydroxy group of cellulose are substituted with acyl groups. The cellulose acylate is preferably any one of cellulose acetate propionate (hereinafter referred to as CAP) and cellulose triacetate (hereinafter referred to as TAC).

 以上のように、上記構成によれば、ふわふわ感があり、空気を多量に含むので、優れた断熱性能がある。そのため、例えば、床、壁、及び天井用の断熱建材、及び車両用断熱部材などへの利用ができる。さらに、上記構成によれば、従来の断熱材よりも熱伝導率が低く、狭いスペースにおいても十分に断熱効果が発揮される。そのため、電子機器、車載機器、及び産業機器の内部に使用する断熱材としての利用が可能である。繊維径が細く、嵩高く、そして、優れた吸音性能があるから、住宅用、車両用、及び電気製品用の吸音材として好適である。また上記構成によれば、十分な通気性が得られるため、特開2017-82346号公報に記載されるように多孔質吸音材(フェルト、グラスウール、及びウレタンフォームなど)上への積層により、吸音性能が向上する。 As described above, according to the above configuration, there is a fluffy feeling and a large amount of air, so that there is excellent heat insulation performance. Therefore, it can be used for, for example, heat insulating building materials for floors, walls, and ceilings, and heat insulating members for vehicles. Furthermore, according to the said structure, heat conductivity is lower than the conventional heat insulating material, and the heat insulation effect is fully exhibited even in a narrow space. Therefore, it can be used as a heat insulating material used inside electronic equipment, in-vehicle equipment, and industrial equipment. Since the fiber diameter is thin, bulky and has excellent sound absorbing performance, it is suitable as a sound absorbing material for homes, vehicles and electrical products. Further, according to the above configuration, sufficient air permeability can be obtained. Therefore, as described in JP-A-2017-82346, sound absorption is achieved by laminating on a porous sound absorbing material (felt, glass wool, urethane foam, etc.). Performance is improved.

 上記構成によれば、平均孔径分布が狭いため、固体と液体との混合物(固体液体混合物)から目的とする物質を分離または除去するためのフィルタとして好適に利用することができる。そのようなフィルタの中でも、特に好ましく用いることができるフィルタは、異物の混入(コンタミネーション)が懸念され、高精度な分離性能が要求される、食品(飲料を含む)用、医療用、超純水用、及び高純度薬液用のフィルタである。ふわふわ感があり空隙率が高いことにより、目詰まりしにくく、圧力損失が小さいことも利点としてある。具体的には、飲料から微粒子及び/または微生物を除去する除去用フィルタ、工業用純水の前処理ろ過フィルタ、血液や唾液などの体液から特定の細胞を捕集する検査用フィルタなどが挙げられる。検査用フィルタとしては、例えば、血糖値検査、尿糖検査、生活習慣病検査、遺伝子検査、腫瘍マーカー検査、及び、血液検査などの検査用フィルタなどがある。 According to the above configuration, since the average pore size distribution is narrow, it can be suitably used as a filter for separating or removing a target substance from a mixture of solid and liquid (solid liquid mixture). Among such filters, filters that can be particularly preferably used are for food (including beverages), medical, and ultrapure, where there is concern about contamination (contamination) and high precision separation performance is required. It is a filter for water and high-purity chemicals. Due to the fluffy feeling and the high porosity, it is difficult to clog and the pressure loss is small. Specific examples include a filter for removing fine particles and / or microorganisms from beverages, a pretreatment filter for industrial pure water, and a test filter for collecting specific cells from body fluids such as blood and saliva. . Examples of the test filter include a test filter for blood glucose level test, urine sugar test, lifestyle-related disease test, genetic test, tumor marker test, blood test, and the like.

 不織布10は、例えば図3に示す不織布製造設備20により製造することができる。不織布製造設備20は、電界紡糸法を用いてファイバ11の形成及び不織布10の製造をするためのものである。不織布製造設備20は、溶液調製部21と不織布製造装置22とを備える。なお、不織布製造装置22の詳細は別の図面に図示しており、図4においては、不織布製造装置22の一部のみを図示している。 The nonwoven fabric 10 can be manufactured by, for example, the nonwoven fabric manufacturing facility 20 shown in FIG. The nonwoven fabric manufacturing facility 20 is for forming the fiber 11 and manufacturing the nonwoven fabric 10 using an electrospinning method. The nonwoven fabric manufacturing facility 20 includes a solution preparation unit 21 and a nonwoven fabric manufacturing apparatus 22. The details of the nonwoven fabric manufacturing apparatus 22 are shown in another drawing, and in FIG. 4, only a part of the nonwoven fabric manufacturing apparatus 22 is shown.

 溶液調製部21は、ファイバ11を形成する溶液25を調製するためのものである。溶液調製部21は、ファイバ11になるファイバ材としてのセルロース系ポリマー15を、溶媒26に溶解することにより、溶液25を調製する。この溶液25が、後述のノズル27a~27cのそれぞれから吐出され、支持体28上でファイバ11を形成する。なお、以降の説明において、ノズル27aとノズル27bとノズル27cとを区別しない場合には、ノズル27と記載する。 The solution preparation unit 21 is for preparing the solution 25 that forms the fiber 11. The solution preparation unit 21 prepares the solution 25 by dissolving the cellulose polymer 15 as a fiber material to be the fiber 11 in the solvent 26. The solution 25 is discharged from each of nozzles 27a to 27c described later, and forms the fiber 11 on the support 28. In the following description, when the nozzle 27a, the nozzle 27b, and the nozzle 27c are not distinguished, they are referred to as a nozzle 27.

 溶媒26の蒸発速度をV(単位はml/s、ミリリットル/秒)とするときに、蒸発速度Vと支持体28上に形成されるファイバ11の平均径DFとは、1≦V/DF≦10を満たす。2≦V/DF≦9であることがより好ましく、3≦V/DF≦8であることがさらに好ましい。V/DFは、蒸発速度Vと平均径DFとの少なくとも一方を調整することにより上記範囲にする。 When the evaporation rate of the solvent 26 is V (unit: ml / s, milliliter / second), the evaporation rate V and the average diameter DF of the fiber 11 formed on the support 28 are 1 ≦ V / DF ≦ 10 is satisfied. More preferably, 2 ≦ V / DF ≦ 9, and further preferably 3 ≦ V / DF ≦ 8. V / DF is set to the above range by adjusting at least one of the evaporation rate V and the average diameter DF.

 蒸発速度Vは、下記の式(1)で求められる。Cは、溶液25の濃度(単位は%)である。濃度Cは、ファイバ材の質量をM1とし、溶媒の質量をM2とするときに、{M1/(M1+M2)}×100の算出式で求める。この例では、M1はセルロース系ポリマー15の質量、M2は溶媒26の質量である。Qはノズル27からの溶液25の吐出量(1時間あたりに吐出される体積であり、単位はml/h、ミリリットル/時)である。ρ2は、溶液25の密度(単位はg/ml)である。したがって、蒸発速度Vは、濃度Cと吐出量Qと密度ρ2との少なくともいずれかひとつを増減することにより調整することができる。蒸発速度Vは、また、溶媒26の処方(例えば、溶媒26を複数成分の混合物とした場合の成分割合など)を調整することによっても、調整することができる。また、平均径DFは、吐出量Qと、濃度Cと、後述する印加電圧と、ノズル27から支持体28までの距離Lとの少なくともいずれかひとつを増減することにより調整することができる。なお、本例では、ノズル27と支持体28との間の空間である紡糸空間の温度を概ね25℃にしているので、蒸発速度Vは、紡糸空間の温度に概ね同じく、25℃で求めている。
   V={(1-0.01C)×Q×10-3}/(3600×ρ2) ・・・(1)
The evaporation rate V is obtained by the following equation (1). C is the concentration of the solution 25 (unit:%). The concentration C is obtained by a calculation formula of {M1 / (M1 + M2)} × 100, where the mass of the fiber material is M1 and the mass of the solvent is M2. In this example, M1 is the mass of the cellulosic polymer 15, and M2 is the mass of the solvent 26. Q is the discharge amount of the solution 25 from the nozzle 27 (the volume discharged per hour, the unit is ml / h, milliliter / hour). ρ2 is the density of the solution 25 (unit: g / ml). Therefore, the evaporation rate V can be adjusted by increasing or decreasing at least one of the density C, the discharge amount Q, and the density ρ2. The evaporation rate V can also be adjusted by adjusting the formulation of the solvent 26 (for example, the component ratio when the solvent 26 is a mixture of a plurality of components). The average diameter DF can be adjusted by increasing or decreasing at least one of the ejection amount Q, the concentration C, the applied voltage described later, and the distance L from the nozzle 27 to the support 28. In this example, the temperature of the spinning space, which is the space between the nozzle 27 and the support 28, is approximately 25 ° C., and therefore the evaporation rate V is obtained at 25 ° C., approximately the same as the temperature of the spinning space. Yes.
V = {(1-0.01C) × Q × 10 −3 } / (3600 × ρ2) (1)

 溶媒26は、1種類の化合物で構成されていてもよいし、2種類以上の化合物で構成されていてもよい。ただし、溶媒26は、ファイバ材を溶解する観点の他に、蒸発速度Vを調整する機能をもつから、蒸発速度Vを調整する観点では、2種類以上の化合物で構成された混合物である方が好ましい。本例の溶媒26も混合物としており、複数の化合物を含有する。例えば、第1化合物26aとしてジクロロメタンを用い、第2化合物26bとしてメタノールを用いている。なお、第1化合物26aと第2化合物26bとに加えて、第1化合物26a及び第2化合物26bと異なる他の化合物を第3化合物,第4化合物,・・・として用い、3種類以上の化合物で溶媒26を構成してもよい。 The solvent 26 may be composed of one kind of compound or may be composed of two or more kinds of compounds. However, since the solvent 26 has a function of adjusting the evaporation rate V in addition to the viewpoint of dissolving the fiber material, the solvent 26 is a mixture composed of two or more kinds of compounds from the viewpoint of adjusting the evaporation rate V. preferable. The solvent 26 of this example is also a mixture and contains a plurality of compounds. For example, dichloromethane is used as the first compound 26a, and methanol is used as the second compound 26b. In addition to the first compound 26a and the second compound 26b, other compounds different from the first compound 26a and the second compound 26b are used as the third compound, the fourth compound,. The solvent 26 may be configured as follows.

 溶媒26は、沸点が90℃以下であることが好ましい。なお、溶媒26が複数の化合物の混合物である場合には、質量割合が最も多い化合物の沸点を、溶媒26の沸点としてみなす。なお、溶媒26が3種以上の化合物の混合物であり、質量割合が最も多い化合物が複数ある場合には、それらのうち沸点が最も高い化合物の沸点を溶媒26の沸点とみなす。例えば、溶媒26が化合物aと化合物bと化合物cとの混合物であり、(化合物aの質量):(化合物bの質量):(化合物cの質量)=40:40:20というように、質量割合が最も多い化合物が化合物aと化合物bとの2つである場合には、化合物aと化合物bとのうち沸点が高い一方の沸点を溶媒26の沸点とみなす。溶媒26は有機化合物であること、すなわち有機溶媒であることが好ましい。 Solvent 26 preferably has a boiling point of 90 ° C. or lower. In addition, when the solvent 26 is a mixture of a plurality of compounds, the boiling point of the compound having the largest mass ratio is regarded as the boiling point of the solvent 26. In addition, when the solvent 26 is a mixture of three or more types of compounds and there are a plurality of compounds having the largest mass ratio, the boiling point of the compound having the highest boiling point is regarded as the boiling point of the solvent 26. For example, the solvent 26 is a mixture of the compound a, the compound b, and the compound c, and (mass of the compound a) :( mass of the compound b) :( mass of the compound c) = 40: 40: 20 When the compound having the largest ratio is the compound a and the compound b, the boiling point of the compound a and the compound b having the higher boiling point is regarded as the boiling point of the solvent 26. The solvent 26 is preferably an organic compound, that is, an organic solvent.

 セルロース系ポリマー15としてセルロースアシレートを用いる場合には、溶媒26に、メタノール、エタノール、イソプロパノール、ブタノール、ベンジルアルコール、アセトン、メチルエチルケトン、シクロヘキサノン、メチルアセテート、エチルアセテート、プロピルアセテート、ブチルアセテート、ギ酸メチル、ギ酸エチル、ヘキサン、シクロヘキサン、ジクロロメタン、クロロホルム、四塩化炭素、ベンゼン、トルエン、キシレン、ジメチルホルムアミド、N-メチルピロリドン、ジエチルエーテル、ジオキサン、テトラヒドロフラン、1-メトキシ-2-プロパノールなどを用いることができる。これらは、単独で使用してもよいし、2種類以上を混合して使用してもよい。 When cellulose acylate is used as the cellulose polymer 15, the solvent 26 is methanol, ethanol, isopropanol, butanol, benzyl alcohol, acetone, methyl ethyl ketone, cyclohexanone, methyl acetate, ethyl acetate, propyl acetate, butyl acetate, methyl formate, Ethyl formate, hexane, cyclohexane, dichloromethane, chloroform, carbon tetrachloride, benzene, toluene, xylene, dimethylformamide, N-methylpyrrolidone, diethyl ether, dioxane, tetrahydrofuran, 1-methoxy-2-propanol and the like can be used. These may be used singly or in combination of two or more.

 また、ファイバ材として、PMMAを用いる場合には、溶媒26に、メタノール、ジクロロメタン、クロロホルム、トルエン、アセトン、テトラヒドロフランなどを用いることができる。これらも、単独で使用してもよいし、2種類以上を混合して使用してもよい。 Further, when PMMA is used as the fiber material, methanol, dichloromethane, chloroform, toluene, acetone, tetrahydrofuran, or the like can be used as the solvent 26. These may also be used alone or in combination of two or more.

 支持体28上のファイバ11の含水率は、3.0%以上、すなわち少なくとも3.0%であることが好ましい。含水率は、3.0%以上10.0%以下の範囲内であることがより好ましく、4.0%以上9.0%以下の範囲内であることが好ましく、5.0%以上8.0%以下の範囲内であることがさらに好ましい。 The moisture content of the fiber 11 on the support 28 is preferably 3.0% or more, that is, at least 3.0%. The water content is more preferably in the range of 3.0% to 10.0%, and preferably in the range of 4.0% to 9.0%, and preferably 5.0% to 8.%. More preferably, it is in the range of 0% or less.

 この例において、不織布製造設備20は、溶液調製部21と不織布製造装置22とを接続する配管33a~33cを備え、不織布製造装置22は、互いに離間した状態に配されたノズル27a~27cを有する。配管33a~33cは、溶液25を案内するためのものである。配管33aは溶液調製部21とノズル27aとを接続し、配管33bは溶液調製部21とノズル27bとを接続し、配管33cは溶液調製部21とノズル27cとを接続する。これにより、ノズル27a~27cのそれぞれから溶液25が出される。ノズル27a~27cから出た溶液25は、それぞれファイバ11を形成する。なお、以降の説明において、配管33aと配管33bと配管33cとを区別しない場合には、配管33と記載する。 In this example, the nonwoven fabric manufacturing facility 20 includes pipes 33a to 33c that connect the solution preparation unit 21 and the nonwoven fabric manufacturing apparatus 22, and the nonwoven fabric manufacturing apparatus 22 has nozzles 27a to 27c arranged in a state of being separated from each other. . The pipes 33a to 33c are for guiding the solution 25. The pipe 33a connects the solution preparation unit 21 and the nozzle 27a, the pipe 33b connects the solution preparation unit 21 and the nozzle 27b, and the pipe 33c connects the solution preparation unit 21 and the nozzle 27c. Thereby, the solution 25 is discharged from each of the nozzles 27a to 27c. The solutions 25 exiting from the nozzles 27a to 27c form the fibers 11, respectively. In the following description, when the pipe 33a, the pipe 33b, and the pipe 33c are not distinguished, they are described as the pipe 33.

 この例では、ファイバ11の捕集及び堆積(以下、これらをまとめて集積と称する)と不織布10の支持とに長尺の支持体28を用いており、この支持体28を長手方向に移動させている。支持体28の詳細については別の図面を用いて後述するが、図3における横方向は支持体28の幅方向であり、図3の紙面奥行方向が支持体28の移動方向である。ノズル27a~27cはこの順で、支持体28の幅方向に並べて配してある。この例では、ノズル27を3本としているが、ノズル27の本数はこれに限られない。なお、配管33a~33cのそれぞれには溶液25をノズル27へ送るポンプ38が設けられている。ポンプ38の回転数を変えることにより、ノズル27a~27cから出る溶液25の各吐出量が調節される。 In this example, a long support 28 is used to collect and deposit the fibers 11 (hereinafter collectively referred to as accumulation) and to support the nonwoven fabric 10, and the support 28 is moved in the longitudinal direction. ing. Although details of the support 28 will be described later with reference to another drawing, the horizontal direction in FIG. 3 is the width direction of the support 28, and the depth direction in FIG. 3 is the moving direction of the support 28. The nozzles 27a to 27c are arranged in this order in the width direction of the support 28. In this example, the number of nozzles 27 is three, but the number of nozzles 27 is not limited to this. Each of the pipes 33a to 33c is provided with a pump 38 for sending the solution 25 to the nozzle 27. By changing the number of rotations of the pump 38, each discharge amount of the solution 25 discharged from the nozzles 27a to 27c is adjusted.

 ノズル27a~27cは保持部材41により保持されている。この保持部材41とノズル27とにより、不織布製造装置22のノズルユニット42が構成される。 The nozzles 27a to 27c are held by a holding member 41. The holding member 41 and the nozzle 27 constitute a nozzle unit 42 of the nonwoven fabric manufacturing apparatus 22.

 不織布製造装置22について、図4を参照しながら説明する。図4には、図3のノズル27a側から見た場合を図示しており、ノズル27についてはノズル27aのみを図示している。不織布製造装置22は、チャンバ45と、前述のノズルユニット42と、集積部50と、電源51等を備える。 The nonwoven fabric manufacturing apparatus 22 will be described with reference to FIG. FIG. 4 shows a case when viewed from the nozzle 27 a side of FIG. 3, and for the nozzle 27, only the nozzle 27 a is illustrated. The nonwoven fabric manufacturing apparatus 22 includes a chamber 45, the above-described nozzle unit 42, a stacking unit 50, a power source 51, and the like.

 チャンバ45は、例えば、ノズルユニット42と、集積部50の一部などを収容している。チャンバ45は密閉可能に構成されており、これにより溶媒ガスが外部に洩れることを防止している。溶媒ガスは、溶液25の溶媒26が気化したものである。 The chamber 45 accommodates, for example, the nozzle unit 42 and a part of the stacking unit 50. The chamber 45 is configured to be hermetically sealed, thereby preventing the solvent gas from leaking to the outside. The solvent gas is obtained by vaporizing the solvent 26 of the solution 25.

 チャンバ45は、内部の相対湿度(以下、単に湿度と称する)を調整する湿度調整機構45aを備えている。湿度調整機構45aは、湿度を調整した気体(例えば空気)をチャンバ45に送り、チャンバ45内の雰囲気を回収した後、再度、湿度を調整してからチャンバ45へ送る。このようにしてチャンバ45の内部の湿度が調整される。この湿度調整は、前述の紡糸空間の湿度を調整するために行われる。すなわち、チャンバ45は、紡糸空間を外部空間から仕切り、紡糸空間の湿度を調整する機能ももっている。ただし、紡糸空間の湿度の調整は、チャンバ45を用いる本例の手法に限定されない。例えば、チャンバ45内に、紡糸空間をチャンバ45内において画定するチャンバによって、紡糸空間の湿度を調整してもよい。 The chamber 45 includes a humidity adjusting mechanism 45a that adjusts the internal relative humidity (hereinafter simply referred to as humidity). The humidity adjusting mechanism 45 a sends a gas (for example, air) whose humidity has been adjusted to the chamber 45, collects the atmosphere in the chamber 45, adjusts the humidity again, and sends it to the chamber 45. In this way, the humidity inside the chamber 45 is adjusted. This humidity adjustment is performed to adjust the humidity of the spinning space described above. That is, the chamber 45 has a function of partitioning the spinning space from the external space and adjusting the humidity of the spinning space. However, the adjustment of the humidity of the spinning space is not limited to the method of this example using the chamber 45. For example, the humidity of the spinning space may be adjusted by a chamber that defines the spinning space in the chamber 45.

 紡糸空間の湿度は、10%以上30%以下であることが好ましい。なお、湿度は、この範囲内であれば、ファイバ11の形成及び不織布10の製造中において変化しても構わない。紡糸空間の湿度は、15%以上25%以下の範囲内であることがより好ましい。 The spinning space humidity is preferably 10% or more and 30% or less. The humidity may change during the formation of the fiber 11 and the production of the nonwoven fabric 10 as long as it is within this range. The humidity of the spinning space is more preferably in the range of 15% to 25%.

 ノズルユニット42はチャンバ45内の上部に配される。ノズル27の溶液25が出る先端は、図4におけるノズル27の下方に配したコレクタ52へ向けてある。溶液25がノズル27の先端に形成されている開口(以下、先端開口と称する)から出る際に、先端開口には溶液25によって概ね円錐状のテイラーコーン53が形成される。 The nozzle unit 42 is disposed in the upper part of the chamber 45. The tip from which the solution 25 of the nozzle 27 exits is directed to the collector 52 disposed below the nozzle 27 in FIG. When the solution 25 exits from an opening formed in the tip of the nozzle 27 (hereinafter referred to as a tip opening), a generally conical Taylor cone 53 is formed by the solution 25 in the tip opening.

 集積部50は、ノズル27の下方に配される。集積部50は、コレクタ52と、コレクタ回転部56と、支持体供給部57と、支持体巻取部58とを有する。コレクタ52はノズル27から出た溶液25を誘引し、形成されたファイバ11を不織布10として捕集するためのものであり、本実施形態では、後述の支持体28上に捕集する。 The stacking unit 50 is disposed below the nozzle 27. The stacking unit 50 includes a collector 52, a collector rotating unit 56, a support supply unit 57, and a support winding unit 58. The collector 52 attracts the solution 25 from the nozzle 27 and collects the formed fiber 11 as the nonwoven fabric 10, and in this embodiment, collects it on a support 28 described later.

 コレクタ52は、金属製の帯状物で環状に形成された無端ベルトで構成されている。コレクタ52は、電源51によって電圧が印加されることにより帯電する素材から形成されていればよく、例えばステンレス製とされる。コレクタ回転部56は、一対のローラ61,62と、モータ60などから構成されている。コレクタ52は、一対のローラ61,62に水平に掛け渡されている。一方のローラ61の軸にはチャンバ45の外に配されたモータ60が接続されており、ローラ61を所定速度で回転させる。この回転によりコレクタ52は移動し、ローラ61とローラ62との間で循環する。本実施形態においては、コレクタ52の移動速度は、例えば0.2m/minとしているが、これに限定されない。 The collector 52 is composed of an endless belt formed in a ring shape with a metal strip. The collector 52 may be made of a material that is charged when a voltage is applied by the power supply 51, and is made of, for example, stainless steel. The collector rotating unit 56 includes a pair of rollers 61 and 62, a motor 60, and the like. The collector 52 is stretched horizontally around the pair of rollers 61 and 62. A motor 60 disposed outside the chamber 45 is connected to the shaft of one roller 61 and rotates the roller 61 at a predetermined speed. This rotation causes the collector 52 to move and circulate between the rollers 61 and 62. In the present embodiment, the moving speed of the collector 52 is, for example, 0.2 m / min, but is not limited thereto.

 コレクタ52には、支持体供給部57によって、帯状の例えばアルミニウムシートからなる支持体28が供給される。支持体28は、ファイバ11を集積し、不織布10を得るためのものである。支持体供給部57は送出軸57aを有する。送出軸57aには支持体ロール63が装着される。支持体ロール63は支持体28が巻芯64に巻き取られて構成されている。支持体巻取部58は巻取軸67を有する。巻取軸67はモータ(図示無し)により回転され、セットされる巻芯68に、不織布10が形成された支持体28を巻き取る。このように、この不織布製造装置22は、ファイバ11を形成する機能と、不織布10を形成する機能とをもつ。なお、支持体28は、コレクタ52上に載せ、コレクタ52の移動によって移動させてもよい。 The collector 52 is supplied with a support 28 made of, for example, an aluminum sheet by a support supply unit 57. The support 28 is for collecting the fibers 11 and obtaining the nonwoven fabric 10. The support body supply unit 57 has a delivery shaft 57a. A support roll 63 is attached to the delivery shaft 57a. The support roll 63 is configured by winding the support 28 around a winding core 64. The support winding unit 58 has a winding shaft 67. The winding shaft 67 is rotated by a motor (not shown), and the support body 28 on which the nonwoven fabric 10 is formed is wound around the core 68 to be set. Thus, this nonwoven fabric manufacturing apparatus 22 has a function of forming the fiber 11 and a function of forming the nonwoven fabric 10. The support 28 may be placed on the collector 52 and moved by moving the collector 52.

 なお、コレクタ52の上にファイバ11を直接集積することにより不織布10を形成してもよいが、コレクタ52を形成する素材またはコレクタ52の表面状態等によっては不織布10が貼り付いてこれを剥がしにくい場合がある。このため、本実施形態のように、不織布10が貼り付きにくい支持体28をコレクタ52上に案内し、この支持体28上にファイバ11を集積することが好ましい。 The nonwoven fabric 10 may be formed by directly collecting the fibers 11 on the collector 52. However, depending on the material forming the collector 52 or the surface state of the collector 52, the nonwoven fabric 10 is stuck and is difficult to peel off. There is a case. For this reason, it is preferable to guide the support body 28 on which the nonwoven fabric 10 is difficult to adhere to the collector 52 as in this embodiment, and to integrate the fiber 11 on the support body 28.

 電源51は、ノズル27とコレクタ52とに電圧を印加し、これにより、ノズル27を第1の極性に帯電させ、コレクタ52を第1の極性と逆極性の第2の極性に帯電させる電圧印加部である。帯電したノズル27内を通過することにより、溶液25が帯電し、帯電した状態でノズル27から出る。なお、この例では保持部材41とノズル27とを導通させており、電源51を保持部材41に接続することにより、保持部材41を介してノズル27に電圧を印加しているが、ノズル27への電圧の印加の手法はこれに限られない。例えばノズル27の各々に電源51を接続することにより各ノズル27に電圧を印加してもよい。本実施形態ではノズル27をプラス(+)に帯電させ、コレクタ52をマイナス(-)に帯電させているが、ノズル27とコレクタ52との極性は逆であってもよい。なお、コレクタ52側をアースして電位を0としても良い。帯電により、テイラーコーン53からは溶液25が紡糸ジェット69としてコレクタ52に向かって噴出される。なお、この例ではノズル27に電圧を印加することにより溶液25を帯電させているが、配管33において溶液25を帯電させ、帯電した状態の溶液2をノズル27に案内してもよい。 The power supply 51 applies a voltage to the nozzle 27 and the collector 52, thereby charging the nozzle 27 to the first polarity and charging the collector 52 to the second polarity opposite to the first polarity. Part. By passing through the charged nozzle 27, the solution 25 is charged and exits the nozzle 27 in a charged state. In this example, the holding member 41 and the nozzle 27 are electrically connected, and the voltage is applied to the nozzle 27 via the holding member 41 by connecting the power source 51 to the holding member 41. The method of applying the voltage is not limited to this. For example, a voltage may be applied to each nozzle 27 by connecting a power source 51 to each nozzle 27. In this embodiment, the nozzle 27 is charged positively (+) and the collector 52 is negatively charged (−). However, the polarity of the nozzle 27 and the collector 52 may be reversed. The collector 52 side may be grounded and the potential may be set to zero. Due to the charging, the solution 25 is ejected from the Taylor cone 53 toward the collector 52 as a spinning jet 69. In this example, the solution 25 is charged by applying a voltage to the nozzle 27, but the solution 25 may be charged in the pipe 33 and the charged solution 2 may be guided to the nozzle 27.

 ノズル27とコレクタ52との距離Lは、セルロース系ポリマー15と溶媒26との種類と、溶液25における溶媒26の質量割合等によって異なるが、30mm以上500mm以下の範囲内が好ましく、本実施形態では例えば150mmとしている。 The distance L between the nozzle 27 and the collector 52 varies depending on the type of the cellulosic polymer 15 and the solvent 26, the mass ratio of the solvent 26 in the solution 25, and the like, but is preferably in the range of 30 mm or more and 500 mm or less. For example, it is 150 mm.

 ノズル27とコレクタ52とに印加する電圧(印加電圧)は、5kV以上200kV以下が好ましい。ファイバ11をより細く形成する観点では印加電圧はこの範囲内でなるべく高いほうが好ましい。本実施形態では例えば40kVとしている。 The voltage (applied voltage) applied to the nozzle 27 and the collector 52 is preferably 5 kV or more and 200 kV or less. From the viewpoint of forming the fiber 11 thinner, the applied voltage is preferably as high as possible within this range. In this embodiment, it is 40 kV, for example.

 不織布製造設備20の作用を説明する。ノズル27と、循環移動するコレクタ52とには、電源51により電圧が印加される。これにより、ノズル27は第1の極性としてのプラスに帯電し、コレクタ52は第2の極性としてのマイナスに帯電する。ノズル27には、溶液調製部21から溶液25が連続的に供給され、移動するコレクタ52上には、支持体28が連続的に供給される。溶液25は、ノズル27a~27cのそれぞれを通過することにより第1の極性であるプラスに帯電し、帯電した状態で、ノズル27a~27cの各先端開口から出る。 The operation of the nonwoven fabric manufacturing facility 20 will be described. A voltage is applied by the power source 51 to the nozzle 27 and the collector 52 that circulates and moves. As a result, the nozzle 27 is positively charged as the first polarity, and the collector 52 is negatively charged as the second polarity. The solution 25 is continuously supplied from the solution preparation unit 21 to the nozzle 27, and the support 28 is continuously supplied onto the moving collector 52. The solution 25 is charged positively as the first polarity by passing through each of the nozzles 27a to 27c, and exits from the tip openings of the nozzles 27a to 27c in a charged state.

 コレクタ52は、第1の極性に帯電した状態で先端開口から出た溶液25を誘引する。これにより、先端開口にはテイラーコーン53が形成され、このテイラーコーン53から紡糸ジェット69がコレクタ52に向かって出る。第1の極性に帯電している紡糸ジェット69は、コレクタ52に向かう間に、自身の電荷による反発でより細い径に分裂し、及び/または螺旋状の軌道を描きながらより細い径に伸びていき、支持体28上にファイバ11が捕集される。ファイバ11は極めて短い時間で堆積するから、不織布10として捕集されることになる。なお、堆積量を増減することにより、不織布10の厚みを調整することができる。堆積量の増減は、例えば、支持体28の移動速度を調整することにより行うことができる。 The collector 52 attracts the solution 25 that has exited from the tip opening while being charged to the first polarity. As a result, a Taylor cone 53 is formed at the tip opening, and the spinning jet 69 exits from the Taylor cone 53 toward the collector 52. The spinning jet 69 charged to the first polarity splits into a smaller diameter due to repulsion due to its own charge and / or extends to a smaller diameter while drawing a spiral trajectory while heading toward the collector 52. The fiber 11 is collected on the support 28. Since the fiber 11 is deposited in a very short time, it is collected as the nonwoven fabric 10. In addition, the thickness of the nonwoven fabric 10 can be adjusted by increasing / decreasing the deposition amount. For example, the amount of deposition can be increased or decreased by adjusting the moving speed of the support 28.

 1≦V/DF≦10であるから、平均径DFが0.10μm以上5.00μm以下の範囲内のファイバ11が形成され、空隙率が90%以上であり、平均孔径DAが0.5μm以上50μm以下の範囲内であり、孔径の標準偏差が1.5μm以下に抑えられた不織布10が得られる。具体的には、1≦V/DFであることにより、V/DF<1の場合と比べて、紡糸ジェット69が細くなり、そのため溶媒26が十分に蒸発し、平均径DFが上記範囲内のファイバ11となって支持体28に到達する。その結果、ファイバ11は、支持体28上において、互いに非接着の状態、あるいは接着してもその接着力が極めて小さい状態で堆積する。その結果、空隙率が90%以上であり、平均孔径DAが0.5μm以上50μm以下の範囲内であり、孔径の標準偏差が1.5μm以下に抑えられた不織布10となる。V/DF≦10であることにより、10<V/DFの場合と比べて、紡糸ジェット69は、ビーズ(微小球)にならずにファイバ11を確実に形成し、捕集される。ビーズが形成されないから、ビーズが支持体28上の不織布10の空隙13を埋めてしまうこともない。その結果、空隙率は確実に90%以上になる。 Since 1 ≦ V / DF ≦ 10, the fiber 11 having an average diameter DF of 0.10 μm or more and 5.00 μm or less is formed, the porosity is 90% or more, and the average pore diameter DA is 0.5 μm or more. The non-woven fabric 10 having a pore diameter standard deviation of 1.5 μm or less is obtained within a range of 50 μm or less. Specifically, by satisfying 1 ≦ V / DF, the spinning jet 69 becomes thinner than in the case of V / DF <1, so that the solvent 26 is sufficiently evaporated and the average diameter DF is within the above range. It becomes the fiber 11 and reaches the support 28. As a result, the fibers 11 are deposited on the support 28 in a non-adhered state with each other or in a state in which the adhesive force is extremely small even when bonded. As a result, the nonwoven fabric 10 has a porosity of 90% or more, an average pore diameter DA in the range of 0.5 μm to 50 μm, and a standard deviation of the pore diameter of 1.5 μm or less. By satisfying V / DF ≦ 10, the spinning jet 69 reliably forms the fiber 11 and does not become beads (microspheres) as compared with the case of 10 <V / DF. Since the beads are not formed, the beads do not fill the gap 13 of the nonwoven fabric 10 on the support 28. As a result, the porosity is surely 90% or more.

 紡糸空間は、10%以上30%以下の湿度に調整されているから、支持体28上のファイバ11の含水率が確実に3.0%以上になり、また、10%より大きくならない。支持体28上のファイバ11の含水率が3.0%以上であることにより、3.0%未満である場合に比べて、以降生成した紡糸ジェット69はより確実に、ファイバ11として支持体28上に集積し、堆積する。これは、支持体上37に捕集されたファイバ11が含有する水分によって電荷を逃がすアースの機能を担うようになり、そのため、以降紡糸空間で生成した紡糸ジェット69は周辺への飛散が抑制された状態で支持体28へ向かい、ファイバ11となって到達するからと考えられる。また、ファイバ11の含水率が3.0%以上であることにより、1≦V/FD≦10であることと相まって、不織布10は、より確実に、90%以上の空隙率で製造される。含水率が10%以下であることにより、10%よりも大きい場合に比べて、吸湿したファイバ11が自重によって変形することが抑えられ、空隙が高く維持されやすい。 Since the spinning space is adjusted to a humidity of 10% or more and 30% or less, the moisture content of the fiber 11 on the support 28 is surely 3.0% or more, and does not exceed 10%. Since the moisture content of the fiber 11 on the support 28 is 3.0% or more, the spinning jet 69 generated thereafter is more reliably formed as the fiber 28 as compared with the case where it is less than 3.0%. Accumulate and deposit on top. This serves as an earth function for releasing electric charges due to moisture contained in the fiber 11 collected on the support 37, and therefore, the spinning jet 69 generated in the spinning space is suppressed from scattering to the periphery. In this state, it is considered that the fiber 11 is reached toward the support 28. In addition, when the moisture content of the fiber 11 is 3.0% or more, coupled with 1 ≦ V / FD ≦ 10, the nonwoven fabric 10 is more reliably manufactured with a porosity of 90% or more. When the moisture content is 10% or less, compared to the case where the moisture content is larger than 10%, the fiber 11 that has absorbed moisture is prevented from being deformed by its own weight, and the gap is easily maintained high.

 沸点が90℃以下である溶媒26を用いることにより、沸点が90℃よりも高い溶媒26を用いた場合に比べて、紡糸ジェット69から溶媒26がより蒸発しやすく、かつ過度な蒸発が抑制される。また、溶媒26として有機溶媒を用いることにより、例えば水を用いた場合に比べて、紡糸ジェット69は湿度が調整されている紡糸空間を通過する間に、適度な量の溶媒26を蒸発し、かつ、紡糸空間と水分のバランスを保つ。その結果、ファイバ11の乾燥の度合いと含水率とのバランスがとりやすい。 By using the solvent 26 having a boiling point of 90 ° C. or lower, the solvent 26 is more easily evaporated from the spinning jet 69 and excessive evaporation is suppressed as compared with the case where the solvent 26 having a boiling point higher than 90 ° C. is used. The Further, by using an organic solvent as the solvent 26, the spinning jet 69 evaporates an appropriate amount of the solvent 26 while passing through the spinning space in which the humidity is adjusted, as compared with the case where water is used, for example. And keep the balance of spinning space and moisture. As a result, it is easy to balance the degree of drying of the fiber 11 and the moisture content.

 ファイバ11はふわふわ感がある不織布10を形成し、支持体28とともに支持体巻取部58に送られる。不織布10は、支持体28と重なった状態で巻芯68に巻かれる。巻芯68は巻取軸67から取り外された後に、支持体28から不織布10が分離される。このようにして得られた不織布10は長尺であるが、この後、例えば所望のサイズに切断してもよい。 The fiber 11 forms the fluffy nonwoven fabric 10 and is sent to the support winding portion 58 together with the support 28. The nonwoven fabric 10 is wound around the core 68 in a state where it overlaps the support 28. After the winding core 68 is removed from the winding shaft 67, the nonwoven fabric 10 is separated from the support 28. The nonwoven fabric 10 thus obtained is long, but after that, for example, it may be cut into a desired size.

 この例では、コレクタ52として循環移動するベルトを用いたが、コレクタはベルトに限定されない。例えば、コレクタは固定式の平板であってもよいし、円筒状の回転体としてもよい。平板や円筒体からなるコレクタの場合にも、不織布10をコレクタから容易に分離することができるように支持体28を用いることが好ましい。なお、回転体を用いる場合には、回転体の周面にファイバからなる筒状のシート材が形成されるため、紡糸後に回転体から筒状のシート材を抜き取り、所望の大きさ及び形状にカットすればよい。 In this example, a circulating belt is used as the collector 52, but the collector is not limited to a belt. For example, the collector may be a fixed flat plate or a cylindrical rotating body. Also in the case of a collector made of a flat plate or a cylindrical body, it is preferable to use the support 28 so that the nonwoven fabric 10 can be easily separated from the collector. When a rotating body is used, a cylindrical sheet material made of fibers is formed on the peripheral surface of the rotating body. Therefore, after spinning, the cylindrical sheet material is extracted from the rotating body, and is formed into a desired size and shape. Cut it out.

 上記の例では、先端開口を下向きにした姿勢でノズル27を配し、ノズル27の下にコレクタ52を配しており、これにより、溶液25を下向きに吐出している。ただし、溶液25の吐出の方向はこの例に限られない。例えば、先端開口を上向きにした姿勢でノズル27を配し、かつ、コレクタ52をノズル27の上に配することにより、溶液25を上向きに吐出してもよい。 In the above example, the nozzle 27 is disposed with the tip opening facing downward, and the collector 52 is disposed under the nozzle 27, whereby the solution 25 is discharged downward. However, the discharge direction of the solution 25 is not limited to this example. For example, the solution 25 may be discharged upward by disposing the nozzle 27 with the tip opening facing upward and disposing the collector 52 on the nozzle 27.

  [実施例1]~[実施例8]
 不織布製造設備20を用いて、表1に示す各条件で不織布10を製造し、実施例1~8とした。製造した不織布10の厚みは、前述の通り4000μmである。用いたファイバ材は、表1の「ファイバ材」欄に記載している。
[Example 1] to [Example 8]
Using the nonwoven fabric manufacturing facility 20, the nonwoven fabric 10 was manufactured under the conditions shown in Table 1, and Examples 1 to 8 were obtained. The thickness of the manufactured nonwoven fabric 10 is 4000 micrometers as above-mentioned. The fiber material used is described in the “fiber material” column of Table 1.

 溶媒26は、第1化合物26aと第2化合物26bとの混合物とした。用いた第1化合物26aと第2化合物26bとは、表1に示す。表1において「DMC」はジクロロメタン、「MeOH」はメタノール、「NMP」はN-メチルピロリドンである。表1の「第1化合物と第2化合物との質量割合」欄は、(第1化合物の質量):(第2化合物の質量)を示しており、例えば、「87:13」とは、(第1化合物の質量):(第2化合物の質量)=87:13であることを意味する。表1の「含水率」は、支持体28上に集積されたファイバ11の含水率である。表1の「孔径の標準偏差」欄においては、小数点以下2桁で求めた値を四捨五入した結果が0.0になる場合には、「<0.1」と記載する。 The solvent 26 was a mixture of the first compound 26a and the second compound 26b. The first compound 26a and the second compound 26b used are shown in Table 1. In Table 1, “DMC” is dichloromethane, “MeOH” is methanol, and “NMP” is N-methylpyrrolidone. The "mass ratio of the first compound and the second compound" column in Table 1 indicates (mass of the first compound) :( mass of the second compound). For example, "87:13" It means that the mass of the first compound) :( the mass of the second compound) = 87: 13. “Moisture content” in Table 1 is the moisture content of the fiber 11 integrated on the support 28. In the column “Standard deviation of pore diameter” in Table 1, when the result of rounding off the value obtained with two decimal places is 0.0, “<0.1” is entered.

 得られた不織布10を2本の指で繰り返し押す動作をした場合の弾力感であるふわふわ感は、下記の圧縮率の評価と対応していた。具体的には、ふわふわ感がより感じられるほど、圧縮比が高かった。そこで、圧縮率をふわふわ感の評価として実施した。 The fluffiness, which is the elasticity when the obtained nonwoven fabric 10 is repeatedly pressed with two fingers, corresponds to the following compression rate evaluation. Specifically, the compression ratio was higher as more fluffy feeling was felt. Therefore, the compression ratio was evaluated as an evaluation of fluffiness.

 圧縮率は以下の方法で評価した。まず、不織布10から10cm×10cmのサイズをサンプルとして切り出した。このサンプルを、第1表面10Aを上向きした状態で静置し、第1表面10Aに質量800gの重りを載せ、載せた状態のサンプルの厚みをノギスで測定した。いずれのサンプルも、重りを外した場合には、第1表面10Aが元の高さに戻り、形が復元した。重りを載せる前の厚み(4000μm)を載せた状態の厚みで除算した値を圧縮比とした。圧縮比は表1に示す。 The compression rate was evaluated by the following method. First, a size of 10 cm × 10 cm was cut out from the nonwoven fabric 10 as a sample. The sample was allowed to stand with the first surface 10A facing upward, a weight of 800 g was placed on the first surface 10A, and the thickness of the loaded sample was measured with calipers. In any sample, when the weight was removed, the first surface 10A returned to the original height, and the shape was restored. The compression ratio was obtained by dividing the thickness before loading the weight (4000 μm) by the thickness of the loaded state. The compression ratio is shown in Table 1.

Figure JPOXMLDOC01-appb-T000001
Figure JPOXMLDOC01-appb-T000001

 さらに、実施例1で得られた不織布10を使用し、遺伝子検査を行った。具体的には、実施例1で得られた不織布10によりヒト全血をろ過した後、不織布10上に残った白血球細胞を使用し、特許4058508号公報の明細書段落[0057]~[0061]に記載される方法に従って遺伝子検査を行った。その結果、特許4058508号公報に記載される実施例と同様の結果が得られた。 Furthermore, genetic testing was performed using the nonwoven fabric 10 obtained in Example 1. Specifically, after filtering human whole blood with the nonwoven fabric 10 obtained in Example 1, white blood cells remaining on the nonwoven fabric 10 are used, and paragraphs [0057] to [0061] in the specification of Japanese Patent No. 4058508 are disclosed. Genetic testing was performed according to the method described in. As a result, the same result as the example described in Japanese Patent No. 4058508 was obtained.

  [比較例1]~[比較例2]
 表1に示す条件で不織布を製造し、比較例1~2とした。
[Comparative Example 1] to [Comparative Example 2]
Nonwoven fabrics were produced under the conditions shown in Table 1 and designated as Comparative Examples 1 and 2.

 実施例と同様の方法及び基準で、圧縮比をふわふわ感として評価した。評価結果は表1に示す。 The compression ratio was evaluated as fluffy by the same method and standard as in the examples. The evaluation results are shown in Table 1.

 10  不織布
 10A 第1表面
 11  ファイバ
 13  空隙
 15  セルロース系ポリマー
 20  不織布製造設備
 21  溶液調製部
 22  不織布製造装置
 25  溶液
 26  溶媒
 26a 第1化合物
 26b 第2化合物
 27a~27c ノズル
 28  支持体
 33a~33c 配管
 38  ポンプ
 41  保持部材
 42  ノズルユニット
 45  チャンバ
 45a 湿度調整機構
 50  集積部
 51  電源
 52  コレクタ
 53  テイラーコーン
 56  コレクタ回転部
 57  支持体供給部
 57a 送出軸
 58  支持体巻取部
 60  モータ
 61,62  ローラ
 63  支持体ロール
 64  巻芯
 67  巻取軸
 68  巻芯
 69  紡糸ジェット
 D1 径
 L  距離
DESCRIPTION OF SYMBOLS 10 Nonwoven fabric 10A 1st surface 11 Fiber 13 Space | gap 15 Cellulosic polymer 20 Nonwoven fabric manufacturing equipment 21 Solution preparation part 22 Nonwoven fabric manufacturing apparatus 25 Solution 26 Solvent 26a 1st compound 26b 2nd compound 27a-27c Nozzle 28 Support body 33a-33c Piping 38 Pump 41 Holding member 42 Nozzle unit 45 Chamber 45a Humidity adjustment mechanism 50 Accumulation part 51 Power supply 52 Collector 53 Taylor cone 56 Collector rotation part 57 Support body supply part 57a Delivery shaft 58 Support body winding part 60 Motor 61, 62 Roller 63 Support body Roll 64 Winding core 67 Winding shaft 68 Winding core 69 Spinning jet D1 Diameter L Distance

Claims (12)

 平均径が0.10μm以上5.00μm以下の範囲内であるファイバを備え、空隙率が少なくとも90%であり、平均孔径が0.5μm以上50μm以下の範囲内であり、かつ、孔径の標準偏差が大きくても1.5μmである不織布。 Provided with a fiber having an average diameter in the range of 0.10 μm to 5.00 μm, a porosity of at least 90%, an average pore diameter in the range of 0.5 μm to 50 μm, and a standard deviation of the pore diameter A non-woven fabric that is 1.5 μm at most.  前記ファイバは、セルロース系ポリマーで形成されている請求項1に記載の不織布。 The nonwoven fabric according to claim 1, wherein the fiber is formed of a cellulose-based polymer.  溶媒にファイバ材が溶解している溶液とコレクタとの間に電圧を印加し、前記溶液をノズルから前記コレクタへ噴出することによりファイバを形成するファイバ形成方法において、
 前記溶媒の蒸発速度をVμl/sとし、前記ファイバの平均径をDFμmとするときに、1≦V/DF≦10であるファイバ形成方法。
In a fiber forming method of forming a fiber by applying a voltage between a solution in which a fiber material is dissolved in a solvent and a collector, and ejecting the solution from the nozzle to the collector,
A fiber forming method in which 1 ≦ V / DF ≦ 10 when the evaporation rate of the solvent is V μl / s and the average diameter of the fiber is DF μm.
 前記ファイバの含水率を少なくとも3.0%にする請求項3に記載のファイバ形成方法。 The fiber forming method according to claim 3, wherein a moisture content of the fiber is set to at least 3.0%.  前記ノズルと前記コレクタとの間の紡糸空間の相対湿度を10%以上30%以下にすることにより、前記ファイバの前記含水率を調整する請求項3または4に記載のファイバ形成方法。 The fiber forming method according to claim 3 or 4, wherein the moisture content of the fiber is adjusted by adjusting a relative humidity of a spinning space between the nozzle and the collector to 10% or more and 30% or less.  前記紡糸空間は、内部の相対湿度を調整する湿度調整機構を備えるチャンバにより、外部空間と仕切られている請求項5に記載のファイバ形成方法。 The fiber forming method according to claim 5, wherein the spinning space is partitioned from the external space by a chamber having a humidity adjusting mechanism for adjusting an internal relative humidity.  前記ファイバ材は、セルロース系ポリマーである請求項3ないし6のいずれか1項に記載のファイバ形成方法。 The fiber forming method according to any one of claims 3 to 6, wherein the fiber material is a cellulosic polymer.  前記セルロース系ポリマーは、セルロースアシレートである請求項7に記載のファイバ形成方法。 The fiber forming method according to claim 7, wherein the cellulose polymer is cellulose acylate.  前記セルロースアシレートは、セルロースアセテートプロピオネートと、セルローストリアセテートとのいずれかである請求項8に記載のファイバ形成方法。 The fiber forming method according to claim 8, wherein the cellulose acylate is either cellulose acetate propionate or cellulose triacetate.  前記溶媒は、複数の化合物の混合物である請求項3ないし9のいずれか1項に記載のファイバ形成方法。 The fiber forming method according to any one of claims 3 to 9, wherein the solvent is a mixture of a plurality of compounds.  前記溶媒は、ジクロロメタンとメタノールとを含有する請求項10に記載のファイバ形成方法。 The fiber forming method according to claim 10, wherein the solvent contains dichloromethane and methanol.  溶媒にファイバ材が溶解している溶液とコレクタとの間に電圧を印加し、前記溶液をノズルから噴出することにより形成したファイバを、前記コレクタ上に不織布として捕集し、
 前記溶媒の蒸発速度をVμl/sとし、前記ファイバの平均径をDFμmとするときに、1≦V/DF≦10である不織布製造方法。
A voltage is applied between the solution in which the fiber material is dissolved in the solvent and the collector, and the fiber formed by ejecting the solution from the nozzle is collected as a nonwoven fabric on the collector,
A non-woven fabric manufacturing method wherein 1 ≦ V / DF ≦ 10, where the evaporation rate of the solvent is V μl / s and the average diameter of the fiber is DF μm.
PCT/JP2019/006503 2018-03-28 2019-02-21 Nonwoven fabric, method for forming fiber, method for manufacturing nonwoven fabric Ceased WO2019187827A1 (en)

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