Patent Application
20160175748
The present invention relates to a multi-layered nanofiber having increased heat resistance and its manufacturing method. More particularly, the present invention relates to the multi-layered nanofiber filter having increased heat resistance by electrospinning polymer on substrate and polymer nanofibers are consecutively laminating and its manufacturing method.
Generally, a filter is a filtering medium which filters out foreign matter in fluid, and comprises a liquid filter and an air filter. An air filter is used for prevention of defective high-tech products along high-tech industry development. Installation in Clean room which completely eliminates biologically harmful things such as dust in air, particles, bio particles such as virus and mold, bacteria, etc. is more prevalent day by day. Clean room is applied in various fields such as production of semiconductor, assembly of computing device, tape manufacture, seal printing, hospital, medicine production, food processing plant, and food and agriculture field.
The air filter forms porous layer with fine porous structure on the surface of a filter medium, performs function of stop penetrating dust into the medium, and filters. However, particles with larger particle size form Filter Cake on the surface of the filter medium. Also, fine particles go through the first surface layer, gradually accumulate in the filter medium, and block pore of the filter. Eventually, particles blocking pore of filter and fine particles increase pressure loss of a filter, decline sustainability of a filter, and with conventional filter medium there is difficulty in filtering fine pollutant particles having 1 micron or less nanosize.
Meanwhile, conventional air filter provides static electricity to fiber-assembly comprising a filter medium, and measures efficiency according to the principle collecting by electrostatic force. However, European Air Filter Test Standard, EN779, revised to eliminate efficiency of filter by static electricity effect in 2012 and revealed that conventional filter actual efficiency decreases 20% or more.
In addition, as glass-fiber which is used as conventional heat-resistant filter material causes bad-influence to the environment, Europe and the United States are in the state of restricting glass-fiber use for environmental safety.
Meanwhile, gas turbine which is a kind of rotary-internal combustion engine generally used in thermal power plant intakes purified air from outside, compresses it, injects compressed air with fuel to combustion burner, mixes them, combusts mixed air and fuel, obtains high temperature and high pressure combustion gas, injects the high temperature and high pressure combustion gas to vane of turbine, and attains rotatory power.
Since the gas turbine comprises very precise component, periodic planned preventive maintenance is held, and wherein the air filter is used for pretreatment to purify air in the atmosphere which inflows to a compressor.
Here, the air filter adopts air for combustion intake to gas turbine, removes foreign substance in atmosphere such as dust, purifies thoroughly, and provides the air to the gas turbine.
Filter currently used in gas turbine has problems such as it is vulnerable to high temperature and foreign matter is not well eliminated.
Moreover, most micro-fiber conventionally produced uses spinning methods such as melt-spinning, dry-spinning, and wet-spinning. In short, polymer solution is forced to spin through fine holes with mechanical force. However, nonwoven fabric manufactured using such method has diameter of approximately 5˜500 μm range, and has difficulty in producing nanofiber 1 μm or less. Therefore, filter comprising fiber with large diameter could filter large polluted particles, but filtering fine polluted particles of nanosize is virtually impossible.
In order to solve the problems stated above, various methods which apply to filter by producing nanosize fiber have been developed. When applying nanofiber to filter, comparing to conventional filter medium having large diameter, specific-surface area is very large, flexibility of surface functionality is good, pore size is nano-level, and harmful fine particles and gas are effectively eliminated.
However, filter using nanofiber has problems such as increasing production cost, difficulty in adjusting various conditions for production. Also, as there is difficulty in mass-production, filter using nanofiber could not be produced and distributed in relatively low unit cost. Moreover, filters currently used in gas turbine, furnace, etc. are required heat-resisting property.
In addition, filters used in gas turbine, furnace, etc. conventionally used glass fiber to satisfy heat-resisting property. However, in Europe and the United States, use of glass fiber is restricted for environmental safety, and other heat-resistant material filter are required, and comparing to conventional filter, filter having more enhanced heat-resisting property is required.
Also, since conventional technology of spinning nano non-woven fabric is limited to small scale production line concentrating on laboratory, there is no concept such as dividing spinning-section into unit or block, and in this case only nano non-woven fabric with even fiber thickness spun. When using the nano non-woven fabric as filter, there are problems such as limitations in permeability and sustainability.
Meanwhile, substrate of conventional filter is cellulose or synthesis-fiber, and developed in method of coating nanofiber on substrate. However, in the case of coating nanofiber on substrate, nanofiber and substrate separation was founded. In order to prevent this, separate adhesives or additives were input, in this case, adjusting spinning condition is difficult and when realization of filter using nanofiber, production cost is increased, difficulty in adjusting various conditions for production. Also, as there is difficulty in mass-production, filter using nanofiber could not be produced and distributed in relatively low unit cost.
Moreover, as conventional technology of spinning nanofiber is limited to small scale production line concentrating on laboratory, there is no concept such as dividing spinning-section into unit or block, and in this case spinning only nanofiber with even thickness. When using the nanofiber as filter, there are problems such as limits in permeability and sustainability.
The present invention is contrived to solve the problems, the purpose is to provide multi-layered nanofiber filter and manufacturing method thereof. The electrospinning polymer on substrate, polymer nanofibers of present invention are consecutively laminating formed, having fine pore and low pressure loss, high efficient and heat-resistant polymer nanofiber filter, and having enhanced heat-resisting property.
In order to achieve the objects stated above, the present invention is multi-layered nanofiber filter for enhanced heat-resisting property, comprising: a substrate; the first heat-resistant polymer nanofiber non-woven fabric laminating formed by electrospinning on the substrate; and the second heat-resistant polymer nanofiber non-woven laminating formed by electrospinning on the first heat-resistant polymer nanofiber non-woven fabric.
Moreover, the present invention is manufacturing method of multi-layered nanofiber filter for enhanced heat-resisting property, comprising: a step of after dissolving the first heat-resistant polymer in organic solvent, the first spinning solution is provided to nozzle connected to a front-end block, and dissolving the second heat-resistant polymer in organic solvent and the second spinning solution is provided to nozzle connected to a rear-end block; a step of electrospinning the first spinning solution on cellulose substrate from nozzle connected to the front-end block, and the first polymer nanofiber non-woven fabric laminating formed; and a step of consecutively electrospinning the second spinning solution on the first polymer nanofiber non-woven fabric from nozzle connected to the rear-end block, and the second polymer nanofiber non-woven fabric laminating formed.
Also, the present invention is manufacturing method of multi-layered nanofiber filter for enhanced heat-resisting property, further comprising: a step of after dissolving polyacrylonitrile in organic solvent and providing polyacrylonitirle solution to a front-end block nozzle, dissolving meta-aramid in organic solvent and providing meta-aramid solution to a middle bock of nozzle, and after dissolving polyamic acid in organic solution and providing polyamic acid solution to a rear-end block of nozzle; a step of electrospinning polyacrylonitrile solution on cellulose substrate from the front-end block of nozzle and laminating formed polyacrylonitrile nanofiber non-woven fabric; a step of electrospinning meta-aramid solution on the polyacrylonitirle nanofiber non-woven fabric from the middle block of nozzle and laminating formed meta-aramid nanofiber non-woven fabric; a step of consecutively electrospinning polyamic acid solution on the meta-aramid nanofiber non-woven fabric from the rear-end block of nozzle and laminating formed polyamic acid nanofiber non-woven fabric; and a step of heat-treatment of the laminated polyamic acid nanofiber non-woven fabric and imidization of polyamic acid nanofiber non-woven fabric.
Moreover, the present invention is manufacturing method of multi-layered nanofiber filter for enhanced heat-resisting property, further comprising: a step of dissolving heat-resistant polymer in organic solution and producing spinning solution; and electrospinning the spinning solution on a substrate and laminating formed heat-resistant polymer nanofiber non-woven fabric.
The multi-layered nanofiber filter according to the present invention has excellent heat-resisting property, simultaneously having fine pore and having low pressure drop and high efficiency. Also, the present invention can realize a new form of high efficient nanofiber filter without causing increase of pressure, and as it has low pressure loss, the filter has excellent durability.
Moreover, the manufacturing method of the multi-layered nanofiber filter according to the present invention uses electrospinning method, thereby having an advantage of efficient manufacturing process as well as having competitive-price.
While this invention has been described in connection with what is presently considered to be practical exemplary embodiments, it is to be understood that the invention is not limited to the disclosed embodiments, but, on the contrary, is intended to cover various modifications and equivalent arrangements included within the spirit and scope of the appended claims.
The present invention describes an electrospinning apparatus manufacturing filter by electrospinning spinning solution on substrate reference to drawings.
Moreover,
In addition,
As illustrated in the drawing, the electrospinning apparatus(10) according to the present invention comprises a spinning solution main tank(not shown) filling spinning solution inside, a metering pump(not shown) for quantitatively supplying polymer spinning solution filled in the spinning solution main tank, a nozzle block(3) arranged a plurality of nozzle(2) which discharge polymer spinning solution in the spinning solution main tank and comprising in pin form, a collector(4) collecting spun and jetted polymer spinning solution which is located and installed over the nozzle block with a predetermined distance apart, and a block(20) holding inside a voltage generator(1a, 1b) which generates voltage to the collector(4), and a case(8) comprising a conductor or a non-conductor in the block(20).
The present invention comprises one spinning solution main tank(not shown), or in the case of comprising two or more spinning solution, two or more spinning solution main tank are provided, or the inside of one spinning solution main tank can be divided in to two or more space, and each of the divided space can be filled and supplied two or more polymer spinning solution.
Moreover, according to an embodiment of the present invention, it uses two spinning solution main tank(not shown). However, the present invention can use one spinning solution main tank, and after dividing the inner space into two, each of the divided space can be each filled and used two different kinds of spinning solution. Moreover, in the case of 3 or more kinds of polymer are used, the inside of a spinning solution main tank can be divided into 3 or more space, and 3 or more spinning solution main tank can be provided and each polymer solution can be provided.
Meanwhile, according to another embodiment of the present invention, it comprises using three spinning solution main tank(not shown), and provided three kinds of polymer solution in each spinning solution main tank. However, it comprises one spinning solution main tank, the inner space is divided in three sections, and each of the section can each be filled and used three kinds of polymer solution.
Here, according to the present invention, the electrospinning apparatus(10) uses a bottom-up electrospinning apparatus which jets spinning solution in upward direction.
Meanwhile, in an embodiment of the present invention, for an electrospinning apparatus, a bottom-up electrospinning apparatus which jets spinning solution in upward direction is used, or a top-down electrospinning apparatus which jets spinning solution in downward direction can be used, or a hybrid electrospinning apparatus which uses both a bottom-up electrospinning apparatus and a top-down electrospinning apparatus can be used, and it does not be limited thereto.
Moreover, the present invention uses two spinning solution main tank(not shown). However, it can use one spinning solution main tank, after dividing the inner space into two sections, and each filling and using two different kinds of spinning solution in each section. Also, in the case of polymer being three or more kinds, the inside of spinning solution main tank can be divided in three or more space, and three or more spinning solution main tank can be provided and each polymer solution can be provided.
According to the structure as stated above, the electrospinning apparatus(10) consecutively quantitatively provides spinning solution filled in the block(20) of spinning solution main tank in a plurality of nozzle(2) provided high voltage through a metering pump, polymer spinning solution provided in the nozzle(2) spin and line-focused on a collector(4) flowing high voltage through the nozzle(2), forms nanofiber non-woven fabric(not shown), and laminating formed nanofiber non-woven fabric and producing filter.
In addition, in the front-end of the electrospinning apparatus(10) jets polymer spinning solution from a block(20), and has a supply roller(11) providing an elongated sheet(not shown) laminating formed nanofiber, and in the rear-end, a winding roller(12) winding an elongated sheet laminating formed nanofiber is provided.
The elongated sheet is provided for nanofiber sagging prevention and carrying. The present invention uses a filter substrate(5) as an elongated sheet, and on the filter substrate(5) polymer spinning solution laminating jets and nanofiber is formed.
In an embodiment of the present invention, the filter substrate(5) is used as an elongated sheet, or release paper or non-woven fabric can be used, and it does not limited thereto.
The elongated sheet is provided for preventing nanofiber from sagging and carrying. The elongated sheet is provided from the supply roller(11) provided in the front-end of the electrospinning apparatus(10) and is wound up on the winding roller(12) provided in the rear-end.
Meanwhile, each of the block(20a, 20b) of the electrospinning apparatus(10) is installed in the elongated sheet's progress direction(a) based on a collector(4). Moreover, between the collector(4) and the elongated sheet, an auxiliary belt(6) is each provided. Through each of the auxiliary belt(6), the elongated sheet collecting in each collector(4) and laminating formed nanofiber is carried in parallel direction. In other words, the auxiliary belt(6) synchronizes and rotates in feed speed of the elongated sheet, and having a roller for auxiliary belt(7) for driving the auxiliary belt(6). The roller for auxiliary belt(7) is an automatic roller with very small frictional force and the number is two or more. Since the auxiliary belt(6) is provided between the collector(4) and the elongated sheet, the elongated sheet does not attract to the collector applied high voltage and is smoothly carried.
According to the structure as stated above, in a spinning solution main tank of the block(20) of the electrospinning apparatus, filled spinning solution jets on an elongated sheet located on a collector through a nozzle(2), and on the elongated sheet, jetted spinning solution is collected and laminating formed nanofiber non-woven fabric. In addition, according to rotation of the roller for auxiliary belt provided in both sides of the collector(4), an auxiliary belt(6) is driven and an elongated sheet is carried, and located in a block(20b) in the rear-end of the electrospinning apparatus(10), and the process is repeatedly performed.
Meanwhile, a nozzle block(3) as illustrated in
To begin with, the spinning solution storing tank(44) which supplies and stores spinning solution and is connected to the spinning solution main tank supplies spinning solution on a nozzle(2) through a spinning solution circulation pipe(45) by the metering pump(not shown) and progress in spinning. Here, a pipe(43) comprising a plurality of nozzle(2) in series is provided the same spinning solution from the spinning solution storing tank(44). Also, a plurality of the spinning solution main tank is provided, and each is provided with different kind of polymer, and can supply different kind of spinning solution to each pipe(43) and spin.
When spinning from an outlet of the plurality of nozzle(2), solution which could not be spun and overflowed is carried to an overflow solution storing tank(41). The overflow solution storing tank(41) is connected to the spinning solution main tank so overflowed solution can be reused in spinning.
Meanwhile, the main control device(30) of the present invention adjusts spinning condition in the overall process of spinning, controls the amount of spinning solution provided in a nozzle block(3), adjusts voltage of a voltage generator(1a, 1b) in each block(20a, 20b), and according to nanofiber non-woven fabric and an elongated sheet thickness measured by a thickness measuring device(9), feed speed of each block(20a, 20b) is controlled.
The thickness measuring device(9) of the present invention is located in the block(20) front-end and rear-end, and nanofiber non-woven fabric is installed in opposite putting laminating formed elongated sheet in between. The thickness measuring device(9) is connected to the main control device(30) which adjusts spinning condition of the electrospinning apparatus(10), based on the value of nanofiber non-woven fabric and an elongated sheet thickness by the thickness measuring device(9), the main control device(30) controls feed speed of each block(20a, 20b). For example, in terms of electrospinning, thickness of nanofiber discharged in the block(20a) located in the front-end is measured thickness deviation, feed speed of the block(20b) located in the rear-end is decreased, and evenly adjusts thickness of nanofiber non-woven fiber. In addition, the main control device(30) increases discharging amount of the nozzle block(3), adjusts voltage intensity of the voltage generator(1a, 1b), increases discharging amount of nanofiber per unit area, and can adjusts uniformed thickness of nanofiber non-woven fabric.
The thickness measuring device(9), according to an ultrasonic measuring method, comprises a thickness measuring portion measuring a pair of ultrasonic wave, longitudinal wave, and transverse wave which measures the distance between laminating formed nanofiber non-woven fabric and an elongated sheet. Also, based on the measured distance according to the pair of ultrasonic wave, thickness of the nanofiber non-woven fabric and the elongated sheet is calculated, and this is described in
The electrospinning apparatus(10) of the present invention does not change feed speed from initial value in the case of deviation of nanofiber non-woven fabric thickness is less than a certain value, and can control to change feed speed from initial value in the case of the deviation is more than a certain value so control of feed speed according to a feed speed control device can be simplified. Also, not only it can control feed speed but also discharging amount of the nozzle block(3) and voltage intensity can be adjusted. In the case of deviation of thickness is less than a certain value, the nozzle block(3) discharging amount and voltage intensity are not changed from initial value, and in the case of the deviation is more than a certain value, discharging amount of the nozzle block(3) and voltage intensity can be controlled not to change from initial value so the nozzle block(3) discharging amount and voltage intensity control can be simplified.
Meanwhile, the block(20) of the electrospinning apparatus(10) comprises the front-end block(20a) located in the front-end and the rear-end block(20b) located in the rear-end according to spinning location. In an embodiment of the present invention, the number of block is limited to 2, but it can comprise 2 or more or 1.
Moreover, hybrid nanofiber comprising 2 or more kinds of polymer spinning solution can be manufactured.
In addition, by differing voltage intensity provided in each of the block(20), nanofiber with different fiber thickness can consecutively laminating formed, and by supplying different polymer spinning solution to each nozzle(2) located in a nozzle block(3) in one block(20), two or more polymer electrospun and laminating formed hybrid nanofiber can be formed.
Also, in the electrospinning apparatus(10) when electrospinning the same kind of polymer from each block(20), fiber thickness of discharged nanofiber non-woven fabric from the block(20) located in the front-end and fiber thickness of discharged nanofiber non-woven fabric from the block(20) located in the rear-end can be different and it can spin. For example, in order to have difference in fiber thickness, voltage intensity provided to each of the block(20) can be different, or even though adjusting space between the nozzle(2) and the collector(4), nanofiber non-woven fabric with different thickness can be formed, in the case of spinning solution is the same and supply voltage is the same, according to the principle that nearer spinning distance, thicker fiber diameter and further spinning distance, thinner fiber diameter, nanofiber non-woven fabric with different fiber diameter can be formed. Also, spinning solution concentration can be adjusted, or by adjusting feed speed of an elongated sheet, there can be difference in fiber thickness.
Moreover, in the present invention from each of the block(20a, 20b) the same polymer spinning solution spin, or each of the block(20a, 20b) can spin different kind of polymer spinning solution, or in any one block two or more different polymer spinning solution can be spun. In the case of in each block(20a, 20b) at least two or more kinds of different spinning solution each provided and spun, different kind of polymer nanofiber non-woven fabric can consecutively laminating formed.
Meanwhile, in the rear-end of the electrospinning apparatus(10) of the present invention, a laminating device(19) is installed. The laminating device(19) is provided heat and pressure, through this an elongated sheet and nanofiber non-woven fabric are adhered, winded in a winding roller(12) and produces filter.
By operating electrospinning through the electrospinning method, as illustrated in
Meanwhile, the electrospinning apparatus(10) enlarges collecting area and can uniform nanofiber collecting density. Also, it effectively prevents Droplet Phenomenon, enhances nanofiber quality, enhances effect of fiber formation by electric force, and can mass-produce nanofiber. Also, from the block(20) having a nozzle(2) comprising a plurality of pin, in terms of electrospinning, material and electrospinning condition can be differently adjusted so non-woven fabric and filament width and thickness can be freely modified and adjusted.
In addition, in the case of the electrospinning polymer, even though it is different according to polymer matter, it is the most preferable to electrospinning in environmental condition of temperature permitted limit 30 to 40° C. and humidity 40 to 70%.
In the present invention, nanofiber diameter is preferably from 30 to 1000 nm, and more preferably from 50 to 500 nm.
A description will now be given to polymer used in the present invention.
Heat-resistant polymer resin comprises polymer with the melting point 180° C. or more so even though temperature continuously rises, it doesn't get damaged by melting point. For example, heat-resistant polymer resin comprising heat-resistant polymer extremely fine fiber layer is resin with the melting point 180° C. or more or resin with no melting point such as polyamide, polyimide, polyamide-imide, poly(meta-phenylene isophthalamide), polysulfone, polyether ketone, polyether imide, aromatic polyesters such as polyethylene terephthalate, polytrimethylene terephthalate, polyethylene naphthalate, polyphosphazene kinds such as polytetrafluoroethylene, polydiphenoxyphosphazene, poly-bis[2-(2-methoxyethoxy) phosphazene], polyurethane copolymer including polyurethane and polyether urethane, and cellulose acetate, cellulose acetate butyrate, cellulose acetate propionate. Resin with no melting point refers to resin which doesn't melt though temperature is 180° C. or more and burn out. Also, heat-resistant polymer resin used in the present invention is preferably dissolve in organic solvent for extremely fine fiberize such as electrospinning.
First, polyimide is polymer containing imide group in repeating unit, and has feature of not changing property in wide temperature range from 273° C. below zero to 400° above zero, and mechanical strength and heat-resisting property are very excellent. However, since most polyimide has insolubility property and it is very difficult to process with conventional process so in polyamic acid(PAA) form which is the precursor is generally processed. Therefore, polyimide is manufactured by polymerizing polyamic acid and going through imidization process.
Generally, polyimide is manufactured according to step two reaction. The first step is a step synthesizing polyamic acid, polyamic acid adds and polymerizes dianhydride in reacting solution, in this case, in order to increase polymerization, adjustment in reaction temperature, solvent's water content, and monomer purity is needed. Solvent used in this step is mainly organic polar solvent such as dimethylacetamide(DMAc), dimethylformamide(DMF), and N-methyl-2-pyrrolidone(NMP). For the diamine at least one can be used among 4-4′-oxydianiline(ODA), para-phenylene diamine(p-PDA), and o-phenylene diamine(o-PDA). Also, for the anhydride at least one selected from the group including pyromellitic dianhydride(PMDA), benzophenonetetracarboxylic dianhydiride(BTDA), 4-4′-oxydiphthalic anhydride(ODPA), biphenyl-tetracarboxylic acid dianhydride(BPDA), and bis(3,4-dicarboxyphenyl) dimethylsilane dianhydride(SIDA).
Moreover, weight average molecular weight(Mw) of polyamic acid produced through the method is preferably 10,000 to 500,000. If molecular weight of polyamic acid is less than 10,000, sufficient property for achieving non-woven fabric can't be obtained, and if it is more than 500,000, handling solution is not easy and performance declines.
The second step is a step of dehydration and cyclization reaction producing polyimide from polyamic acid, four methods stated below are representative.
First, reprecipitation method injects polyamic acid solution in excessive amount of poor solvent, and obtains polyamic acid in solid state. For reprecipitation solvent mainly water is used, and toluene or ether are used as cosolvent.
Secondly, chemical imidization method uses acetic anhydride/pyridine as dehydration catalyst, and performs chemically imidization reaction. This method is useful in polyimide film manufacture.
Thirdly, thermal imidization method heats polyamic acid solution in 150 to 350° C., and performs thermally imidization method. The most simple process or degree of crystallization is high, and when using amine solvent, amine exchange reaction occurs so there is drawback such as polymer degradation.
Lastly, isocyanate method uses diisocyanate as monomer instead of diamine, and heating monomer mixture in temperature 120° C. or more, CO2 gas occurs and polyimide is manufactured.
Also, polyacrylonitrile(PAN) means polymer of acrylonitrile(CH2=CHCN).
Here, polyacrylonitrile resin is copolymer made from mainly mixture of acrylonitrile and monomer. Mostly used monomer is butadiene styrene vinylidene chloride or other vinyl compound, etc. Acrylic fiber comprises at least 85% of acrylic nitrile, and modacrylic including 35 to 85% of acrylonitrile. If other monomer is included, fiber has feature of increasing chemical affinity regarding dye. Specifically, with respect to acrylonitrile-based copolymer and spinning solution manufacture, in the case of producing using acrylonitrile-based copolymer, in the process of producing micro fiber in electrospinning method, less nozzle contamination, excellent electrospinning, increasing solubility of solvent, and better mechanical properties. Also, polyacrylonitrile softening point is 300° C. or more, and heat-resisting property is excellent.
Moreover, polyacrylonitrile polymerization degree is 1,000 to 1,000,000, and preferably 2,000 to 1,000,000.
Also, polyacrylonitrile is preferably used in the realm satisfying acrylonitrile monomer, hydrophobic monomer, and hydrophilic monomer usage amount. When polymerization of polymer, acrylonitrile monomer weight % is hydrophilic monomer weight % and hydrophobic monomer weight % ratio is 3:4, in the case of the value subtracted from the total monomer is less than 60, viscosity is too low for electrospinning, wherein even though inputting cross-linker, it causes contamination of nozzle and difficult to form stable JET when electrospinning.
Also, in the case of the value if 90 or more, spinning viscosity is so high that it is difficult to spinning, wherein even though inputting additives which can low viscosity, diameter of micro fiber is thicken, productivity of electrospinning is so low that it can not achieve the object of the present invention.
In addition, in acrylic polymer, more comonomer is inputted, the amount of cross-linker should be more input in order to achieve stability in electrospinning and prevent nanofiber mechanical property degradation.
The hydrophobic monomer is preferably to use any one or more selected from ethylene-based compound such as methacrylate, ethyl acrylate, methyl methacrylate, ethyl methacrylate, butyl methacrylate, vinyl acetate, vinyl pyrrolidone, vinylidene chloride, and vinyl chloride, and derivatives thereof.
The hydrophilic monomer is preferably to use any one or more selected from among ethylene-based compound and polyfunctional acid such as acrylic acid, allyl alcohol, meta-allyl alcohol, hydroxyethyl acrylate, hydroxyethyl methacrylate, hydroxypropyl acrylate, butanediol monoacrylate, dimethylaminoethyl acrylate, butenetricarboxylic acid, vinyl sulfonic acid, allyl sulfonic acid, methallyl sulfonic acid, and parastyrene sulfonic acid, and derivatives thereof.
Initiator used for producing the acrylonitrile-based polymer is azo compound or sulfate compound, but generally it is preferable to use radical initiator used in oxidation-reduction reaction.
Meanwhile, the heat-resistant polymer used in the present invention is preferable to use polyether sulfone.
Generally, polyethersulfone(PES) is amber transparent non-crystalline resin having repeating unit, generally produced according to condensation polymerization of dichlorodiphenyl sulfone.
Polyether sulfone is super heat-resistant engineering plastic developed by the British ICI Corp, among thermoplastic it is polymer having very excellent heat-resisting property. Since polyether sulfone is non-crystalline, there is less property degradation by temperature rise, and because of less temperature dependency of flexural modulus, in minus 100° C. to 200° C., it almost doesn't change. Distortion temperature under load is 200 to 220° C., and glass transition temperature is 225° C. Also, creep resistance within 180° C. is the most excellent among thermoplastic resin, and have properties to withstand hot water of 150° C. to 160° C. or stream.
Due to the properties, polyether sulfone is used in optical disc, magnetic disk, in electrical and electronic field, in hydrothermal field, in automobile field, and heat-resisting for paint.
Also, solvent usable with the polyether sulfone is acetone, tetrahydrofuran, methylene chloride, chloroform, N-Dimethylformamide(DMF), N-Dimethylacetamide(DMAc), N-methyl pyrrolidone(NMP), cyclohexane, water, or their mixture, and it does not limited thereto.
Moreover, the description examines polyamide used in the present invention.
Polyamide is polymer connected to amide bond(—CONH—), and can be obtained by condensation polymerization of diamine and di-acid. Polyamide differs characteristic according to amide bond in molecular structure, and according to amidogen ration, property is modified. For example, if ratio of amidogen in molecular increases, specific gravity, the melting point, absorbency, rigidity, etc. also increases.
In addition, because of polyamide excellent properties in corrosion resistance, wear resistance, chemical resistance, and insulating properties, it is applied in various fields such as for clothing, tire cord, carpet, rope, computer ribbon, parachute, plastic, adhesive, etc.
In general polyamide is classified aromatic polyamide and aliphatic polyamide, representative aliphatic polyamide is nylon. Nylon is originally the U.S. DuPont Corp brand name, but currently it is used as nonproprietary name.
Nylon is hygroscopic polymer, and reacts sensitive to temperature. Representative nylon is nylon 6, nylon 66, and nylon 46, etc.
First, nylon 6 has excellent properties in heat-resisting property, formability, and chemical resistance. In order to produce it, ring-opening polymerization of ε-Caprolactam is used. Nylon 6 is named because the carbon number of caprolactam is six.
Meanwhile, nylon 66 and nylon 6 have similar properties in general, but comparing to nylon 6, nylon 66 heat-resisting property is very excellent, and it is polymer excellent in self-extinguishability and wear resistance. Nylon 66 is produced by dehydration condensation polymerization of hexamethylenediamine adipic acid.
Also, nylon 46 has excellent heat-resisting property, mechanical properties, and shock resistance, and processing temperature is high. Nylon 46 is manufactured by polycondensation of tetramethylenediamine and adipic acid. The raw material diaminobutane(DAB) is produced from reaction of acrylonitrile and hydrogen cyanide. The first step in polymerization process is making salt from diaminobutane and adipic acid, under proper pressure, after polymerization reaction, change to prepolymer, and the prepolymer solid under existence of nitrogen and water vapor, processed in approximately 250° C., and produced in a solid state being polymerization.
Especially, nylon 6 has excellent properties in regular ordered arrangement methylene group and amide group and having high amide concentration. Nylon 46 melting point is approximately 295° C., and it is higher than other nylon types.
Because of the properties, it receives attention as resin having excellent heat-resisting property.
The following examines meta-aramid used in the present invention.
Meta-aramid is the first super heat-resistant aramid fiber, within a short time in 350° C., and when using consecutively, it can be used in 210° C., and if it is exposed in temperature more than this, it melts with other fibers or has properties not combusted but carbonized. Most of all, unlike other products done flame resistance or flame retarding, during carbonization, poisonous gas or harmful substance is not emitted so it also has excellent properties as environmental-friendly fiber.
Moreover, meta-aramid has very strong molecular structure of molecule comprising fiber, its original strength is strong and in spinning step molecule is easily oriented in fiber axis direction, enhances crystallinity, and increases fiber strength.
The meta-aramid portion is 1.3 to 1.4, and preferable to have weight average molecular weight of 300,000 to 1,000,000. The most preferable weight average molecular weight is 3,000 to 500,000. Also, it includes meta-oriented synthetic aromatic polyamide. Polymer should have fiber-forming molecular weight, and primary can include aromatic polyamide homopolymer, copolymer and mixture thereof, wherein at least 85% of amide(—CONH—)bond directly attached two aromatic rings. The ring can be unsubstituted or substituted. Polymer having two rings or when radical is meta-oriented with respect to each other according to molecular chain, it becomes meta-aramid. Preferably, copolymer has 10% or less other diamine which substituted primary diamine used in forming polymer, or having 10% or less other diacid chloride which substituted primary diacid chloride used in forming polymer. Preferable meta-aramid is poly(meta-phenylene isophthalamide) (MPD-I) and its copolymer. One such meta-aramid fiber is Nomex(registered trademark) aramid fiber available from E. I. du Pont de Nemours and Company in Wilmington, Del., the United States. However, meta-aramid fiber is available in various styles such as Tejinconex(registered trademark) available from Teijin Ltd. Of Tokyo, Japan; New Star(registered trademark) meta-aramid available from Yantai Spandex Co. Ltd of Shandong, China; and Chinfunex(registered trademark) aramid 1313 available from Guangdong Charming Chemical Co. Ltd. of Xinhui, Guangdong, China.
The organic solvent can be used to select any one or more among propylene carbonate, butylene carbonate, 1,4-butyrolactone, diethyl carbonate, dimethyl carbonate, 1,2-dimethoxyethane, 1,3-dimethyl-2-imidazolidinone, dimethyl sulfoxide, ethylene carbonate, ethylmethyl carbonate, N,N-dimethylformamide, N,N-dimethylacetamide, N-methyl-2-pyrrolidone, polyethylene sulfolane, tetraethylene glycol dimethyl ether, acetone, alcohol, or their mixture, and more preferably it is preferred to use dimethylformamide(DMF) or dimethylacetamide(DMAc).
The following description examines inorganic polymer used in the present invention.
Inorganic polymer refers to polymer including inorganic element in polymer main chain or side chain. The inorganic element narrowly means a variety of metal(Ordinary Metals filling s and p orbit such as aluminum and magnesium, Transition Metals filling d orbit such as titanium, zirconium and tungsten, Inner Transition Metals filling f orbit such as lanthanoide-actinoids), and broadly comprising forming framework with non-metallic inorganic elements such as Si, Ge, P, and B elements.
This inorganic polymer can be divided into the following four types.
First, in the case of inorganic component including side chain of inorganic polymer, nature of inorganic polymer is almost maintained, in the case of nature of inorganic component included in side chain is shown, second, in the case of inorganic element is together introduced with carbon in polymer main chain framework or introduced alone, third in the case of organic-inorganic hybrid polymer designed to play a role as precursor for producing ceramic, and forth, in the case of ionic compound having network structure comprising purely inorganic component or lattice structure.
Inorganic polymer started to get attention as in the mid 1980s Yajima of Nippon Carbon used polycarbosilane(PCS) and synthesized SiC fiber(product name: NICALON) which came on the market. Until now it is not used much, but it is a product expected to be used not only in future aerospace and nuclear power field but also in heat-resisting property field of general industrial field. Application method of inorganic polymer as a complex is polymer impregnation and pyrolysis(PIP), this method mixes organic compound such as PCS and silicon carbide powder and after making slurry, the slurry permeates into silicon carbide fiber preform and pyrolyzes, and obtaining silicon carbide matrix. Recently, as development in fiber with excellent heat-resisting property is getting attention, if PIP method is improved by developing new inorganic compound having excellent feature, by increasing pyrolysis temperature, silicon carbide matrix with excellent crystalline and stoichiometric ratio can be produced.
Meanwhile, among various application field of inorganic polymer, ceramic precursor application caused enormous development in high-tech industries field. Especially, Silicon carbide(SiC), silicon nitride(Si3N4), and ceramic are thermally and chemically stable in high temperature, intensity is strong so the use is prevalent in various fields such as defense weapon field like the aerospace, ship, automobile, missile, etc., electrical and electronic, steel industry, nuclear reactor business, machine for shelf building, and sport product manufacture, and it has various industrial use such as for special use, ceramic is manufactured in film or fiber form. Moreover, silicon polymer is economical because raw material is low price and polymerization yield is high, and in molecule Si and C or N ratio can be adjusted variously, and because of high fusibility and solubility, forming processing is possible and in order to increase ceramic remaining yield, cross-linking can be made by various chemical reaction. According to pyrolysis condition, it can be easily selected to silicon carbide, silicon nitride, etc., by pyrolyzing by mixing with metal, cermet also can be produced.
Inorganic polymer used in electrospinning inorganic polymer produces spinning solution which dissolved inorganic polymer in acetone solvent. In this case, number average molecular weight of inorganic polymer is preferably in realm of 5,000 to 100,000.
The inorganic polymer is siloxane or siloxane polymer alone or siloxane group or polymer comprising siloxan copolymer and coupler selected among monomethacrulate, vinyl, hydride, distearate, bis(12-hydroxy-stearate), methoxy, ethoxylated, propoxylated, diglycidyl ether, mono glycidyl ether, mono hydroxy, bis(hydroxyalkyl), chlorine, bis(3-aminopropyl), and bis((amino ethyl-amino propyl)dimethoxy silyl)ether.
The following description explains substrate used in the present invention.
For the substrate, it is preferable to use one kind selected among cellulose substrate, meta-aramid substrate, bicomponent substrate.
First, the cellulose substrate has excellent dimennal stability in high temperature and has feature of high heat-resisting property. Fine cellulose fiber has high crystalline and high modulas of elasticity in regard of forming fine porous structure, and essentially in high temperature dimensional stability is very excellent. Because of such feature, cellulose substrate is used in consumer products such as high performance filter, functional paper, sheet for cooking, and air cleaning sheet, and in technical fields such as semiconductor device, board for wiring board, substrate of low linear coefficient of expansion material, and separator for electric condenser such as capacitor. Also, the cellulose substrate is a natural fiber, and it is an environmental friendly material which can be decomposed after disposal of filter so it reduces additional environment pollution caused by conventional non-biodegradable filter.
Also, meta-aramid substrate has very excellent heat-resisting property because of meta-aramid feature comprising the substrate. Meta-aramid is benzene ring combined with amidogen in meta location, the strength is similar to nylon, but it has advantages such as thermal stability is very excellent, it is lighter compared to other heat-resistant material, and it is possible to absorb. Meta-aramid can be used properly as filter substrate because as it has more operating condition of high temperature, filter stability can be achieved.
Meanwhile, the following description explains the bicomponent substrate. Fiber forming polymer of bicomponent substrate comprising general bicomponent is polyester including polyethylene terephthalate, polyethylene naphthalate, polypropylene terephthalate, polybutylene terephthalate, and the polypropylene terephthalate is such as polytrimethylene terephthalate and polybutylene terephthalate such as polytetramethylene terephthalate.
The bicomponent substrate of the present invention is most preferably polyethylene terephthalate which combined two components with different melting point.
The polyethylene terephthalate bicomponent substrate is core-sheath bicomponent structure comprising polyethylene terephthalate core and low melting point polyethylene terephthalate, in each fiber, sheath is approximately 10 to 90 weight %, and core is approximately 90 to 10 weight %. The sheath works as a thermal bonding agent forming outer surface of binder fiber, having a melting point of approximately 80 to 100° C. The core has a melting point of approximately 160 to 250° C. The following description explains heat adhesive composite fiber in detail providing example of sheath-core type which is a proper realization.
Sheath-core type heat adhesive composite fiber is in sheath portion a conventional melting point analysis instrument and comprising non-crystalline polyester copolymer which doesn't show a melting point, and core component is preferably heat adhesive composite fiber relatively using high melting point component.
Polyester copolymer included in the sheath portion is copolymerization polyester having 50 to 70 mol % of polyethylene terephthalate unit. Also, 30 to 50 mol % is copolymerization acid component and is preferably isophtallic acid, but besides that the usual dicarboxylic acid is all possible.
Moreover, high melting point component used as the core component suitable is polymer with a melting point of 160 or more, and available examples are polyethylene terephthalate, polybutylene terephthalate, polyamide, polyethylene terephthalate copolymer, and polypropylene, etc.
After laminating nanofiber non-woven fabric on the bicomponent substrate(100) and heat-fusing, the sheath portion of the bicomponent substrate(100) is melt, plays a role as adhesive between the substrate and the nanofiber non-woven fabric, and there is an advantage of not needing a separate adhesive.
The following description explains manufacturing method of polyimide nanofiber filter for improved heat-resisting property according to an embodiment of the present invention.
First, in the present invention, for spinning solution polyamic acid is used, and for an elongated sheet a cellulose substrate(100) can be used.
Moreover, polyamic acid solution which dissolved the polyamic acid in organic solvent is provided to a spinning solution main tank of the electrospinning apparatus(10). Polyamic acid solution provided in the spinning solution main tank is consecutively and quantitatively provided to a plurality of nozzle(2) of a nozzle block(3) provided high voltage through a metering pump. Polyamic acid solution provided to each of the nozzle(2) is jetted on the cellulose substrate(100) located on a collector(4) flowing high voltage through the nozzle(2), and forms polyamic acid nanofiber non-woven fabric.
In the present invention, polyamic acid solution is used as the spinning solution, but it does not limited thereto.
Meanwhile, in a front-end block(20a) of the electrospinning apparatus(10), the cellulose substrate(100) laminated polyamic acid nanofiber is carried from the front-end block(20a) to a rear-end block(20b) by a supply roller(11) operated by a motor(not shown) driving and rotation of an auxiliary belt(6) driving by the supply roller(11) rotation, the process is repeated, and forms polyamic acid nanofiber non-woven fabric on the cellulose substrate(100).
In an embodiment of the present invention, instead of an elongated sheet, the cellulose substrate(100) was used, but it is not limited thereto.
Meanwhile, a voltage generator(1a) which provides voltage to the front-end block(20a) provides low spinning voltage, and forms polyamic acid nanofiber non-woven fabric with fiber diameter of 250 to 500 nm on the cellulose substrate(100), and a rear-end voltage generator(1b) which provides voltage to the rear-end block provides high spinning voltage, and laminating forms polyamic acid nanofiber non-woven fabric with fiber diameter of 50 to 250 nm on the polyamic acid nanofiber non-woven fabric with fiber diameter of 250 to 500 nm.
Here, spinning voltage provided by each of the voltage generator(1a, 1b) is 1 kV or more, preferably is 20 kV or more, and voltage provided by the front-end voltage generator(1a) is lower than voltage provided by the rear-end voltage generator(1b).
In the present invention, voltage of the front-end block(20a) of the electrospinning apparatus(10) is provided low, laminating forms polyamic acid nanofiber non-woven fabric with fiber diameter of 250 to 500 nm on substrate, and voltage of the rear-end block(20b) is provided high, laminating forms polyamic acid nanofiber non-woven fabric with fiber diameter of 50 to 250 nm on the polyamic acid nanofiber non-woven fabric with fiber diameter of 250 to 500 nm, and forms polyamic acid nanofiber filter. However, by differing voltage intensity, polyamic acid nanofiber non-woven fabric with fiber diameter of 50 to 250 nm spun in the front-end block(20a), and polyamic acid nanofiber non-woven fabric with fiber diameter of 250 to 500 nm can spin in the rear-end block(20b).
In addition, comprising 3 or more blocks of the electrospinning apparatus(10), differing voltage in each block, and it is possible to produce nanofiber filter laminating forming 3 layer of nanofiber non-woven fabric with different fiber thickness on the bicomponent substrate.
Moreover, by differing voltage intensity provided to each block(20), it is possible to consecutively laminating forming nanofiber non-woven fabric with different fiber thickness, and in one block(20), each nozzle(2) located in a nozzle block(3) supplies different polymer spinning solution, and it is possible to form hybrid nanofiber non-woven fabric electrospun two or more kind polymer together and laminating formed.
Also, by adjusting space between the nozzle(2) and a collector(4), it can form nanofiber non-woven fabric with different thickness, in the case of spinning solution is the same and supply voltage is the same, according to the principle of the nearer spinning distance is, the thicker fiber diameter is, and the farther spinning distance is, the thinner fiber diameter is, it is possible to form nanofiber non-woven fabric with different fiber diameter.
Above this, by comprising two or more kinds of spinning solution polymer, it is possible to produce hybrid nanofiber non-woven fabric.
Therefore, on the cellulose substrate(100), polyamic acid nanofiber non-woven fabric with fiber diameter of 250 to 500 nm is laminating forming, and on the polyamic acid nanofiber non-woven fabric with fiber diameter of 250 to 500 nm, polyamic acid nanofiber non-woven fabric with fiber diameter of 50 to 250 nm is laminating formed, and polyamic acid nanofiber filter is produced.
Polyamic acid nanofiber filter laminating formed according to the process stated above goes through a laminating device(19), becomes thermal imidization, and produces as polyimide nanofiber filter. In the laminating device(19), imidization is performed in 150 to 350° C., and dehydrates polyamic acid nanofiber filter, and produces as polyimide nanofiber filter.
In other words, as the polyamic acid nanofiber filter becomes imidization, on the cellulose substrate(100), a polyimide nanofiber non-woven fabric(200) with fiber diameter of 250 to 500 nm is laminating formed, on the polyimide nanofiber non-woven fabric(200) with fiber diameter of 250 to 500 nm, a polyimide nanofiber non-woven fabric(300) with fiber diameter of 50 to 250 nm laminating formed, and finally polyimide nanofiber filter is produced.
The following description explains manufacture method of multi-layered nanofiber filter for improved heat-resisting property according to another embodiment of the present invention.
First, according to the present invention, meta-aramid solution and polyamic acid solution are used, and as an elongated sheet, a cellulose substrate(100) is used.
In an embodiment of the present invention, instead of an elongated sheet, the cellulose substrate(100) was used, but it is not limited thereto.
Meanwhile, meta-aramid solution which dissolved meta-aramid in organic solvent is provided to a spinning solution main tank connected to a front-end block(20a) located in front-end of the electrospinning apparatus(10), and polyamic acid solution which dissolved polyamic acid in organic solvent is provided to a spinning solution main tank connected to a rear-end block(20b) located in the rear-end. Spinning solution provided to each of the spinning solution main tank is consecutively and quantitatively provided to a plurality of nozzle(2) located in a nozzle block(3) provided high voltage through a metering pump. Each spinning solution provided from each of the nozzle(2) electrospun and line-focused on the cellulose substrate(100) located on the collector(4) flowing high voltage through the nozzle(2).
In the present invention, for the spinning solution meta-aramid solution is used, but it is not limited thereto.
In this case, in order to foster fiber forming by electric force, in the nozzle block(3) and a collector(4) flows voltage of 1 kV or more generated from a voltage generator(1), and more preferably 20 kV or more voltage. Also, for the collector(4), it is more advantageous to use endless belt in terms of productivity. The collector is preferable to do left and right reciprocating motion in predetermined distance to uniform nanofiber density.
Here, in the front-end block(20a) of the electrospinning apparatus(10), the cellulose substrate(100) which electrospun meta-aramid solution and laminated meta-aramid nanofiber carries from the front-end block(20a) to the rear-end block(20b) by a supply roller(11) operated by a motor(not shown) driving and by rotation of an auxiliary belt(6) operated by rotation of the supply roller(11), the process is repeated, and on the cellulose substrate(100), meta-aramid and polyamic acid nanofiber non-woven fabric is formed.
In other words, in the front-end block(20a), on the cellulose substrate(100), meta-aramid nanofiber non-woven fabric(200) which electrospun meta-aramid and laminating formed is formed, and in the rear-end block(20b), on the meta-aramid nanofiber non-woven fabric polyamic acid nanofiber non-woven fabric which electrospun polyamic acid solution and laminating formed is formed.
For the spinning solution, polyamic acid solution is used, but it is not limited thereto.
Moreover, polyamic acid nanofiber non-woven fabric laminating formed by the process stated above goes through laminating device(19), becomes thermal imidization, and produces as polyimide nanofiber non-woven fabric. In the laminating device(19), imidization is performed in 150 to 350° C., dehydrates polyamic acid nanofiber filter, and produces as polyimide nanofiber filter.
Therefore, in other words, the polyamic acid nanofiber non-woven fabric becomes imidization, on the cellulose substrate, meta-aramid nanofiber non-woven fabric(200) laminating formed, on the meta-aramid nanofiber non-woven fabric, polyimide nanofiber non-woven fabric(300) laminating formed, and finally nanofiber filter of the present invention is produced.
The following description explains manufacture method of an inorganic polymer nanofiber filter for improved heat-resisting property according to the other embodiment of the present invention.
First, spinning solution used in the present invention is inorganic polymer, and for an elongated, a substrate(100) is used.
Moreover, inorganic polymer solution which dissolved the inorganic polymer in solvent is provided to a spinning solution main tank of the electrospinning apparatus(10), and inorganic polymer solution provided to the spinning solution main tank is consecutively and quantitatively provided in a plurality of nozzle(2) in a nozzle block(3) provided high voltage and connected to each block(20a, 20b) through a metering pump. Heat-resistant polymer solution provided from each of the nozzle(2) spun and line-focused on the substrate(100) located on the collector(4) flowing high voltage through the nozzle(2), and forms an inorganic polymer nanofiber non-woven fabric.
Here, the following description explains the substrate(100). The substrate(100) can be used preferably cellulose substrate or meta-aramid substrate.
Also, meta-aramid substrate has very excellent heat-resisting property because of meta-aramid features comprising the substrate. Meta-aramid is benzene ring and amidogen combined in meta location. Its strength is similar to the usual nylon, but meta-aramid has advantages such as very excellent thermal stability, lighter than other heat-resistant material, having absorbability. Since operating condition in high temperature can achieve filter stability, it can be properly used as filter substrate.
In an embodiment of the present invention, instead of an elongated sheet, the substrate(100) is used, but it is not limited thereto.
Meanwhile, a front-end voltage generator(1a) providing voltage to the front-end block(20a) provided low spinning voltage, forms an inorganic polymer nanofiber non-woven fabric with fiber diameter of 250 to 500 nm on a substrate(100), a rear-end voltage generator(1b) providing voltage to a rear-end block(20b) provided high spinning voltage, and laminating forming an inorganic polymer nanofiber non-woven fabric with fiber diameter of 50 to 250 nm on the inorganic polymer nanofiber non-woven fabric with fiber diameter of 250 to 500 nm.
Here, spinning voltage provided to each of the voltage generator(1a, 1b) is 1 kV or more, preferably 20 kV or more, and voltage provided by the front-end voltage generator(1a) is lower than voltage provided by the rear-end voltage generator(1b).
According to the present invention, voltage of the front-end block(20a) of the electrospinning apparatus(10) is provided low, laminating forming inorganic polymer nanofiber non-woven fabric with fiber diameter of 250 to 500 nm on substrate, voltage of the rear-end block(20b) is provided high, laminating forming inorganic polymer nanofiber non-woven fabric with fiber diameter of 50 to 250 nm on the inorganic polymer nanofiber non-woven fabric with fiber diameter of 250 to 500 nm, and forms inorganic polymer nanofiber filter. However, by differing voltage intensity, inorganic polymer nanofiber non-woven fabric with fiber diameter of 50 to 250 nm spun in the front-end block(20a), and inorganic polymer nanofiber non-woven fabric with fiber diameter of 250 to 500 nm can be spun in the rear-end block(20b).
Also, comprising 3 or more blocks of the electrospinning apparatus(10), differing voltage of each block(20a, 20b), and it can produce nanofiber filter laminating forming 3 layers of nanofiber non-woven fabric with different fiber thickness on substrate(100).
Moreover, by differing voltage intensity provided to each block(20), nanofiber non-woven fabric with different fiber thickness can be laminating formed, and in one block(20), by providing different polymer spinning solution to each nozzle(2) located in a nozzle block(3), two or more kinds of polymer are together electrospun and laminating formed, and hybrid nanofiber non-woven fabric can be formed.
In addition, in order to differentiate fiber thickness, the method of differing voltage intensity provided to each block(20a, 20b) is used, but by adjusting space between the nozzle(2) and the collector(4) can form nanofiber non-woven fabric with different thickness. In the case of spinning solution is the same and supply voltage is the same, according to the principle of the nearer spinning distance is, the thicker fiber diameter is, and the further spinning distance is, the thinner fiber diameter is, nanofiber non-woven fabric with different fiber diameter can be formed. Also, by adjusting spinning solution concentration, or by adjusting an elongated sheet feed speed, it can differentiate fiber thickness.
Above this, comprising 2 or more kinds of polymer of spinning solution, hybrid nanofiber non-woven fabric can be produced.
Therefore, on the substrate(100), inorganic polymer nanofiber non-woven fabric(200) with fiber diameter of 250 to 500 nm laminating formed, an inorganic polymer nanofiber filter laminating formed inorganic polymer nanofiber non-woven fabric(300) with fiber diameter of 50 to 250 nm on the inorganic polymer nanofiber non-woven fabric(200) with fiber diameter of 250 to 500 nm is produced.
The following description explains manufacturing method of filter medium by using polyether sulfone and polyimide which are heat-resistant polymer resin.
Here, as heat-resistant polymer resin, polyether sulfone and polyimide are used, but it does not limited thereto.
First, the first spinning solution is produced by dissolving polyether sulfone in organic solvent. The first spinning solution is provided to a spinning solution main tank of the electrospinning apparatus(10), and the first spinning solution is consecutively and quantitatively provided to a plurality of nozzle(2) of a nozzle block(3) provided high voltage through a metering pump.
Polyether sulfone solution provided to each of the nozzle(2) spun and line-focused on a collector(4) flowing high voltage through a nozzle(2), sprayed on a meta-aramid substrate(5), and forms polyether sulfone nanofiber. Here, in front-end block(20a) of the electrospinning apparatus(10), a substrate laminated polyether sulfone nanofiber is carried from a front-end block(20a) to a rear-end block(20b) by a supply roller(11) operated by driving of a motor(not shown) and rotation of an auxiliary belt(6) driving by the supply roller(11) rotation.
The second spinning solution provided from the rear-end block(20b) to a main tank injected polyimide precursor solution is consecutively and quantitatively provided to a plurality of nozzle(2) of a nozzle block(3) provided high voltage through a metering pump.
In this case, the front-end block(20a) is called the first supply device, and the rear-end block(20b) is called the second supply device.
More specifically, in the first main tank which stores spinning solution of electrospinning of the present invention stores polyether sulfone spinning solution, and in the second main tank, spinning solution of polyimide precursor resin is stored. The first and second supply device is generally planned to have sealed cylindrical form, and plays a role of providing spinning solution injected consecutively from a spinning solution main tank according to section. A nozzle block is divided into 2 sections, in each section is provided with the first and second supply device, and the first supply device uses polyether sulfone solution, and the second supply device uses polyimide precursor resin solution.
A filter laminating polyether sulfone nanofiber and polyimide nanofiber on produced meta-aramid substrate can extend filter sustainability when using as an air filter of a gas turbine which inflowing high temperature air in air flow direction as using polymer resin with good heat-resisting property.
The length of section divided in the nozzle block can be adjusted according to each layer thickness comprising filter medium.
Also, mechanical properties such as polymer membrane thickness, fiber diameter, and fiber form can be adjusted through controlling electrospinning process conditions such as applied voltage intensity, polymer solution type, viscosity of polymer solution, discharge flow rate.
Desirable electrospinning process condition when spinning solution carried to spinning solution supply pipe is discharged to a collector through a multiple tubular nozzle and forms fiber, nanofiber electrospun from the multiple tubular nozzle widely spreads by sprayed air from a nozzle for air supply, collected on a collector, collecting area becomes wider and integration density is uniform. Excess spinning solution which can't be fiberize in a multiple tubular nozzle is collected from a nozzle for removing overflow, goes through a temporal storage plate of overflow liquid, and again moved to a spinning solution supply plate.
In the case of manufacturing nanofiber, recommended air speed in a nozzle for air supply is 0.05 to 50 m/sec, and more preferably 1 to 30 m/sec. In the case of air speed is less than 0.05 m/sec, distribution of nanofiber collected in a collector is low so collecting area is not largely enhanced, and in the case of air speed is more than 50 m/sec, air speed is so fast that the area line-focused in a collector is decreased, and more seriously not nanofiber but as thick skein form attached to a collector, and nanofiber formation prominently declines.
In addition, spinning solution excessively provided to uppermost part of nozzle block is carried by force to spinning solution main tank by spinning solution discharging device.
In this case, in order to foster fiber forming by electric force, an electric conductor plate installed in lower end of nozzle block and a collector flow voltage generated in voltage generator of 1 kV or more, and more preferably 20 kV or more. For the collector, it is advantageous in terms of productivity to use endless belt. The collector is preferable to do right and left reciprocating motion in predetermined space in order to uniform nanofiber density.
Nanofiber formed on the collector goes through a web supporting roller, wound in a winding roller, and nanofiber manufacturing process is completed.
The manufacturing device widens collecting area, and it can uniform nanofiber integration density, and by effectively preventing droplet phenomenon, quality of nanofiber can be enhanced, fiber forming effect by electric force increases, and can mass-produce nanofiber. Moreover, nozzles comprising a plurality of pin are arranged in block form, and nanofiber's and filament's width and thickness can be modified and adjusted freely.
Also, in the case of spinning heat-resistant polymer, even though it is different according to polymer material, it is the most preferable to spinning in environmental conditions of temperature permitted limit of 30 to 40° C., and humidity of 40 to 70%.
In the present invention, diameter of nanofiber forming multi-layered filter medium is desirable to be 30 to 1,000 nm, and more desirable 50 to 500 nm.
Multi-layered air porosity is desirable to be 40 to 80%, and the smaller fiber diameter is, the smaller pore size is and pore distribution is also smaller. Also, the smaller fiber diameter is, the larger fiber specific surface area is so efficiency of filtering fine particles increases.
The following description explains manufacturing method of filter medium using inorganic polymer and one among heat-resistant polymer resin such as polyacrylonitrile, polyether sulfone, polyimide, polyamide, meta-aramid, and polyvinylidene fluoride.
First, the first spinning solution is produced by dissolving heat-resistant polymer in organic solvent. The first spinning solution is provided to a spinning solution main tank of the electrospinning apparatus(10), and the first spinning solution is consecutively and quantitatively provided to a plurality of nozzle(2) of a nozzle block(3) provided high voltage through a metering pump.
Heat-resistant polymer solution provided to each of the nozzle(2) spun and line-focused on a collector(4) flowing high voltage through a nozzle(2), sprayed on a meta-aramid substrate, and forms meta-aramid nanofiber. Here, in a front-end block(20a) of the electrospinning apparatus(10), a substrate laminated heat-resistant polymer nanofiber is carried from a front-end block(20a) to a rear-end block(20b) by a supply roller(11) operated by a motor(not shown) driving and rotation of an auxiliary belt(6) driving by the supply roller(11) rotation.
The second spinning solution provided from the rear-end block(20b) to a main tank injected inorganic polymer solution is consecutively and quantitatively provided to a plurality of nozzle(2) of a nozzle block(3) provided high voltage through a metering pump.
In this case, the front-end block(20a) is called the first supply device, and the second-end block(20b) is called the second supply device.
More specifically, in the first main tank which stores spinning solution of electrospinning of the present invention stores polymer spinning solution, and in the second main tank, inorganic spinning solution is stored. The first and second supply device is generally planned to have sealed cylindrical form, and plays a role of providing spinning solution injected consecutively from a spinning solution main tank according to section. A nozzle block is divided into 2 sections, in each section is provided with the first and second supply device, and the first supply device uses polymer solution, and the second supply device uses inorganic polymer solution.
A filter laminating inorganic polymer nanofiber and selected on among heat-resistant polymer nanofiber such as polyacrylonitrile, polyether sulfone, polyimide, polyamide, meta-aramid, polyvinylidenefluoride on produced meta-aramid or cellulose substrate when using as air filter of gas turbine inflowing high temperature air in air flow direction, as using polymer resin with good heat-resisting property, it can extend filter sustainability.
The length of section divided in the nozzle block can be adjusted according to each layer thickness comprising filter medium.
Also, mechanical properties such as polymer membrane thickness, fiber diameter, and fiber form can be adjusted through controlling electrospinning process conditions such as applied voltage intensity, polymer solution type, viscosity of polymer solution, discharge flow rate.
Desirable electrospinning process condition when spinning solution carried to spinning solution supply pipe is discharged to a collector through a multiple tubular nozzle and forms fiber, nanofiber electrospun from the multiple tubular nozzle widely spreads by sprayed air from a nozzle for air supply, collected on a collector, collecting area becomes wider and integration density is uniform. Excess spinning solution which can't be fiberize in a multiple tubular nozzle is collected from a nozzle for removing overflow, goes through a temporal storage plate of overflow liquid, and again moved to a spinning solution supply plate.
In the case of manufacturing nanofiber, recommended air speed in a nozzle for air supply is 0.05 to 50 m/sec, and more preferably 1 to 30 m/sec. In the case of air speed is less than 0.05 m/sec, distribution of nanofiber collected in a collector is low so collecting area is not largely enhanced, and in the case of air speed is more than 50 m/sec, air speed is so fast that the area line-focused in a collector is decreased, and more seriously not nanofiber but as thick skein form attached to a collector, and nanofiber formation prominently declines.
In addition, spinning solution excessively provided to uppermost part of nozzle block is carried by force to spinning solution main tank by spinning solution discharging device.
In this case, in order to foster fiber forming by electric force, an electric conductor plate installed in lower end of nozzle block and a collector flow voltage generated in voltage generator of 1 kV or more, and more preferably 20 kV or more. For the collector, it is advantageous in terms of productivity to use endless belt. The collector is desirable to do right and left reciprocating motion in predetermined space in order to uniform nanofiber density.
Nanofiber formed on the collector goes through a web supporting roller, wound in a winding roller, and nanofiber manufacturing process is completed.
The manufacturing device widens collecting area, and it can uniform nanofiber integration density, and by effectively preventing droplet phenomenon, quality of nanofiber can be enhanced, fiber forming effect by electric force increases, and can mass-produce nanofiber. Moreover, nozzles comprising a plurality of pin are arranged in block form, and nanofiber's and filament's width and thickness can be modified and adjusted freely.
Also, in the case of spinning heat-resistant polymer, even though it is different according to polymer material, it is the most desirable to spinning in environmental conditions of temperature permitted limit of 30 to 40° C., and humidity of 40 to 70%.
In the present invention, diameter of nanofiber forming multi-layered filter medium is desirable to be 30 to 1,000 nm, and more desirable 50 to 500 nm.
Multi-layered air porosity is desirable to be 40 to 80%, and the smaller fiber diameter is, the smaller pore size is and pore distribution is also smaller. Also, the smaller fiber diameter is, the larger fiber specific surface area is so efficiency of filtering fine particles increases.
The following description explains manufacturing method of filter comprising nylon nanofiber and bicomponent substrate according to the present invention.
First, in the present invention, nylon is applied as spinning solution, and a bicomponent substrate(100) is applied as an elongated sheet.
Nylon solution which dissolved the nylon in organic solvent is provided to a spinning solution main tank of the electrospinning apparatus(10). Also, nylon solution provided to the spinning solution main tank is consecutively and quantitatively provided to a plurality of nozzle(2) of a nozzle block(3) provided high voltage in each block(20a, 20b) through a metering pump. Nylon solution provided from each of the nozzle(2) is electrospun and line-focused on the bicomponent substrate(100) of an elongated sheet located on a collector(4) flowing high voltage through a nozzle(2), and forms nylon nanofiber non-woven fabric.
Provided though a nozzle(2) of a nozzle block(3) in the block(20), using nylon solution which dissolved nylon applied as spinning solution in organic solvent, and desirably using nylon 6, nylon 46 or nylon 66 solution.
In an embodiment of the present invention uses nylon solution as spinning solution, but it does not limited thereto.
Meanwhile, in the present invention uses a bottom-up electrospinning apparatus which the electrospinning apparatus(10) jets spinning solution in upward direction.
In an embodiment of the present invention uses a bottom-up electrospinning apparatus which jets spinning solution in upward direction, or top-down electrospinning apparatus which jets spinning solution in downward direction can be used, and also a hybrid electrospinning apparatus which uses a bottom-up and top-down electrospinning apparatus together can be used.
In an embodiment of the present invention uses the bicomponent substrate(100) instead of an elongated sheet, but it is not limited thereto.
Here, nylon nanofiber in a front-end block(20a) of the electrospinning apparatus(10) is carried from a front-end block(20a) to a rear-end block(20b) by a supply roller(11) operated by driving of a motor(not shown) and rotation of an auxiliary belt(6) driving by rotation of the supply roller(11), the process is repeated, and on the bicomponent substrate(100) nylon nanofiber non-woven fabric is formed.
In this case, a front-end voltage generator(1a) which provides voltage to the front-end block(20a) provides low spinning voltage, and forms nylon nanofiber non-woven fabric(200) with fiber diameter of 250 to 500 nm on the bicomponent substrate(100), and a rear-end voltage generator(1b) which provides voltage to the rear-end block provides high spinning voltage, and laminating forms nylon nanofiber non-woven fabric(300) with fiber diameter of 50 to 250 nm on the nylon non-woven fabric(200) with fiber diameter of 250 to 500 nm.
Here, spinning voltage provided by each of the voltage generator(1a, 1b) to a nozzle and a collector is 1 kV or more, preferably is 20 kV or more, and voltage provided by the front-end voltage generator(1a) is lower than voltage provided by the rear-end voltage generator(1b).
In the present invention, voltage of the front-end block(20a) of the electrospinning apparatus(10) is provided low, laminating forming nylon non-woven fabric(200) with fiber diameter of 250 to 500 nm on a substrate, and voltage of the rear-end block(20b) is provided high, laminating forming nylon non-woven fabric(300) with fiber diameter of 50 to 250 nm on the nylon non-woven fabric(200) with fiber diameter of 250 to 500 nm, and forms nanofiber filter. However, by differing voltage intensity, nylon nanofiber non-woven fabric(300) with fiber diameter of 50 to 250 nm spun in the front-end block(20a), and nylon nanofiber non-woven fabric(200) with fiber diameter of 250 to 500 nm can spin in the rear-end block(20b).
Also, comprising 3 or more blocks of the electrospinning apparatus(10), differing voltage in each block, and it is possible to produce nanofiber filter laminating forming 3 layer of nanofiber non-woven fabric with different fiber thickness on the bicomponent substrate.
Moreover, by differing voltage intensity provided to each block(20), it is possible to consecutively laminating forming nanofiber non-woven fabric with different fiber thickness, and in one block(20), each nozzle(2) located in a nozzle block(3) supplies different polymer spinning solution, and it is possible to form hybrid nanofiber non-woven fabric electrospun and laminating formed two or more kinds polymer together.
Also, by adjusting space between the nozzle(2) and a collector(4), it can form nanofiber non-woven fabric with different thickness, in the case of spinning solution is the same and supply voltage is the same, according to the principle of the nearer spinning distance is, the thicker fiber diameter is, and the farther spinning distance is, the thinner fiber diameter is, it is possible to form nanofiber non-woven fabric with different fiber diameter.
Above this, by comprising two or more kinds of spinning solution polymer, it is possible to produce hybrid nanofiber non-woven fabric.
Therefore, on the bicomponent substrate(100), a nylon nanofiber non-woven fabric(200) with fiber diameter of 250 to 500 nm laminating formed, and on the nylon nanofiber non-woven fabric(200) with fiber diameter of 250 to 500 nm, nylon nanofiber non-woven fabric(300) with fiber diameter of 50 to 250 nm is laminating formed, and finally a filter comprising nylon nanofiber and a bicomponent substrate is formed, going through a laminating device(19) and thermos compression bonding process, a filter comprising nylon nanofiber and a bicomponent substrate(100) is produced.
The following description explains manufacturing method of multi-layered nanofiber filter for improved heat-resisting property according to an embodiment of the present invention.
First, according to the present invention, for spinning solution, polyacrylonitrile solution, meta-aramid solution, and polyamic acid solution are used, and for an elongated sheet, a cellulose substrate(100) is used.
Moreover, polyacrylonitrile solution which dissolved polyacrylonitrile in organic solvent is provided to a spinning solution main tank connected to a front-end block(20a) located in front-end of the electrospinning apparatus(10), meta-aramid solution which dissolved meta-aramid in organic solvent is provided to a spinning solution main tank connected to a middle block(20b) located in middle of the electrospinning apparatus(10), and polyamic acid solution which dissolved polyamic acid in organic solvent is provided to a spinning solution main tank connected to a rear-end block(20c) located in rear-end of the electrospinning apparatus(10).
In addition, spinning solution provided to each of the spinning solution main tank is consecutively and quantitatively provided to a plurality of nozzle(2) located in a nozzle block(3) provided high voltage through a metering pump. Each spinning solution provided from each of the nozzle(2) spun and line-focused on a collector(4) flowing high voltage through a nozzle(2), and sprayed on a cellulose substrate(100).
In an embodiment of the present invention uses a cellulose substrate(100) instead of an elongated sheet, but it is not limited to this.
Meanwhile, in the electrospinning apparatus(10), in order to facilitate fiber formation by electric force, in a nozzle block(3) and a collector(4) flows voltage of 1 kV or more generated from a voltage generator(1), and more preferably 20 kV or more voltage. Also, for the collector(4), it is more advantageous to use endless belt in terms of productivity. The collector is preferable to do left and right reciprocating motion in predetermined distance to uniform density of nanofiber.
Here, spinning solution spun in a block(20) of the electrospinning apparatus(10) is carried from a front-end block(20a) to a rear-end block(20c) going through a middle block(20b) by a supply roller(11) operated by driving of a motor(not shown) and rotation of an auxiliary belt(6) driving by rotation of the supply roller(11), the process is repeated, and on the cellulose substrate(100) nanofiber non-woven fabric is consecutively laminating formed.
In other words, in the front-end block(20a), on the cellulose substrate(100), polyacrylonitrile solution electrospun and forms laminating formed polyacrylonitrile nanofiber non-woven fabric(200), in middle block(20b), on the polyacrylonitrile nanofiber non-woven fabric(200), meta-aramid solution electrospun and forms laminating formed meta-aramid nanofiber non-woven fabric(300), and in rear-end block(20c), on the meta-aramid nanofiber non-woven fabric(300), polyamic acid solution electrospun and forms laminating formed polyamic acid nanofiber non-woven fabric.
Polyacrylonitrile/meta-aramid/polyamic acid multi-layered nanofiber filter manufactured as stated above goes through a laminating device(19), through thermal imidization, polyamic acid nanofiber non-woven fabric is modified to polyimide nanofiber non-woven fabric(400), and manufactures multi-layered filter of the present invention. The laminating device(19) performs imidization in 150 to 350° C., dehydrates polyamic acid nanofiber non-woven fabric, and produces polyimide nanofiber non-woven fabric.
Therefore, on a cellulose substrate(100), polyacrylonitrile nanofiber non-woven fabric(200), meta-aramid nanofiber non-woven fabric(300), and polyimide nanofiber non-woven fabric are consecutively laminating formed, and a multi-layered nanofiber filter of the present invention is produced.
The following description explains in detail manufacturing method of filter medium forming nanofiber between substrates by using heat-resistant polymer resin.
First, by dissolving the first heat-resistant polymer and the second heat-resistant polymer in organic solvent and produces the first spinning solution and the second spinning solution. The first spinning solution and the second spinning solution are each provided to spinning solution main tank of the electrospinning apparatus(10), and the first spinning solution and the second spinning solution are consecutively and quantitatively provided to a plurality of nozzle(2) of a nozzle block(3) provided high voltage through a metering pump.
The first heat-resistant polymer solution provided to each of the nozzle(2) spun and line-focused on a collector(4) flowing high voltage through a nozzle(2), sprayed on a cellulose substrate or a meta-aramid substrate(5), and forms the first heat-resistant polymer nanofiber. Here, in a front-end block(20a) of the electrospinning apparatus(10), a substrate laminating the first heat-resistant polymer nanofiber is carried from a front-end block(20a) to a rear-end block(20b) by a supply roller(11) operated by driving of a motor(not shown) and rotation of an auxiliary belt(6) driving by rotation of the supply roller(11).
The second spinning solution provided from a rear-end block(20b) to a main tank injected the second heat-resistant polymer solution is consecutively and quantitatively provided to a plurality of nozzle(2) of a nozzle block(3) provided high voltage through a metering pump.
More specifically, in the first main tank which stores spinning solution of electrospinning of the present invention stores the first heat-resistant polymer spinning solution, and in the second main tank, the second heat-resistant polymer spinning solution is stored. The first and second supply device is generally planned to have sealed cylindrical form, and plays a role of providing spinning solution injected consecutively from a spinning solution main tank according to section. A nozzle block is divided into 2 sections, in each section is provided with the first and second supply device, and the first supply device uses the first heat-resistant polymer spinning solution, and the second supply device uses the second heat-resistant polymer spinning solution.
In the present invention, provided low voltage of the front-end block(20a) of the electrospinning apparatus(10), laminating forming nanofiber with thick fiber thickness on a substrate, and voltage of the rear-end block(20b) is provided highly, laminating forming nanofiber with thin fiber thickness on the nanofiber with thick fiber thickness, and forms nanofiber filter. However, by differing voltage intensity, nanofiber with thin fiber thickness spun in the front-end block(20a), and nanofiber with thick fiber thickness can be spun in the rear-end block(20b).
The length of section divided in the nozzle block can be adjusted according to the thickness of each layer comprising filter medium.
In addition, a grounded collector is controlled to move in one-way, consecutive process of forming consecutive nanofiber layer is possible, and the present invention through such process simplifies manufacturing method of both sides filter medium, and increases speed of the production.
Also, mechanical properties such as polymer membrane thickness, fiber diameter, and fiber form can be adjusted through controlling electrospinning process conditions such as applied voltage intensity, polymer solution type, viscosity of polymer solution, discharge flow rate.
Nanofiber on the substrate in the laminating device(19) the conventional substrate and substrate of other materials are covered with cover, and forms nanofiber layer between substrates.
Desirable electrospinning process condition when spinning solution carried to spinning solution supply pipe is discharged to a collector through a multiple tubular nozzle and forms fiber, nanofiber electrospun from the multiple tubular nozzle widely spreads by sprayed air from a nozzle for air supply, collected on a collector, collecting area becomes wider and integration density is uniform. Excess spinning solution which can't be fiberize in a multiple tubular nozzle is collected from a nozzle for removing overflow, goes through a temporal storage plate of overflow liquid, and again moved to a spinning solution supply plate.
In the case of manufacturing nanofiber, recommended air speed in a nozzle for air supply is 0.05 to 50 m/sec, and more preferably 1 to 30 m/sec. In the case of air speed is less than 0.05 m/sec, distribution of nanofiber collected in a collector is low so collecting area is not largely enhanced, and in the case of air speed is more than 50 m/sec, air speed is so fast that the area line-focused in a collector is decreased, and more seriously not nanofiber but as thick skein form attached to a collector, and nanofiber formation prominently declines.
In addition, spinning solution excessively provided to uppermost part of nozzle block is carried by force to spinning solution main tank by spinning solution discharging device.
In this case, in order to foster fiber forming by electric force, an electric conductor plate installed in lower end of nozzle block and a collector flow voltage generated in voltage generator of 1 kV or more, and more preferably 20 kV or more. For the collector, it is advantageous in terms of productivity to use endless belt. The collector is preferable to do right and left reciprocating motion in predetermined space in order to uniform nanofiber density.
Nanofiber formed on the collector goes through a web supporting roller, wound in a winding roller, and nanofiber manufacturing process is completed.
The manufacturing device widens collecting area, and it can uniform nanofiber integration density, and by effectively preventing droplet phenomenon, quality of nanofiber can be enhanced, fiber forming effect by electric force increases, and can mass-produce nanofiber. Moreover, nozzles comprising a plurality of pin are arranged in block form, and nanofiber's and filament's width and thickness can be modified and adjusted freely.
Also, in the case of spinning heat-resistant polymer, even though it is different according to polymer material, it is the most preferable to spinning in environmental conditions of temperature permitted limit of 30 to 40° C., and humidity of 40 to 70%.
In the present invention, diameter of nanofiber forming multi-layered filter medium is desirable to be 30 to 1,000 nm, and more desirable 50 to 500 nm.
The following description explains manufacturing method of polyether sulfone nanofiber for improved heat-resisting property which produced through electrospinning polyether sulfone on a meta-aramid substrate produced using the electrospinning apparatus(10).
First, according to the present invention, polyether sulfone is used as polymer of spinning solution, and a meta-aramid substrate(100) is used as an elongated sheet.
Moreover, polyether sulfone solution which dissolved polyether sulfone in organic solvent is provided to a spinning solution main tank of the electrospinning apparatus(10), and consecutively and quantitatively provided to a nozzle(2) of a nozzle block(3) provided high voltage through a metering pump. Polyether sulfone solution provided from each of the nozzle(2) spun and line-focused on a collector(4) provided high voltage through the nozzle(2), sprayed on the meta-aramid substrate(100), and forms polyether sulfone nanofiber non-woven fabric(200).
In the present invention, for the spinning solution polyether sulfone solution is used.
In an embodiment of the present invention, polyether sulfone solution is used as spinning solution, but it does not limited thereto.
Here, a cellulose substrate laminated polyether sulfone nanofiber in a front-end block(20) of the electrospinning apparatus(10) is carried from a block located in front-end to a block located in rear-end by a supply roller(11) operated by driving of a motor(not shown) and by rotation of an auxiliary belt(6) driving by rotation of the supply roller(11), the process is repeated, and on the meta-aramid substrate(100), polyether sulfone nanofiber nonwoven(200) is formed.
In an embodiment of the present invention, instead of an elongated sheet, the meta-aramid substrate(100) is used, but it does not limited thereto.
Therefore, on the meta-aramid substrate(100), in a block(20) of the electrospinning apparatus(10), electrospinning the polyether sulfone, laminating formed polyether sulfone nanofiber non-woven fabric(200), and a filter of the present invention is produced.
Meanwhile, by differing spinning voltage of a front-end block and a rear-end block of the electrospinning apparatus(10), fiber diameter of nanofiber can be made different. In other words, even though it is the same polyether sulfone nanofiber non-woven fabric, when providing low spinning voltage of the front-end block and providing high spinning voltage of the rear-end block, nanofiber with large fiber diameter and polyether sulfone nanofiber with small fiber diameter can be laminated consecutively on the meta-aramid substrate(100). For example, when provided low voltage of the front-end block, polyether sulfone nanofiber non-woven fabric with thick fiber thickness is formed in the front-end, and when provided high voltage in the rear-end block, polyether sulfone nanofiber non-woven fabric with thin fiber thickness can be formed.
Here, in order to putting difference in fiber thickness of the polyether sulfone nanofiber non-woven fabric(200) and spinning, the method of differentiating voltage intensity provided to each block(20) of the electrospinning apparatus(10) is used, and other methods such as differentiating concentration of spinning solution, or adjusting space between a nozzle(2) and a collector(4), or adjusting feed speed of an elongated sheet is used.
The following description explains manufacturing method of polyimide nanofiber filter for improved heat-resisting property produced by electrospinning polyamic acid on a meta-aramid substrate manufactured by using the electrospinning apparatus(10).
First, in the present invention, polyamic acid is used as polymer of spinning solution, and a meta-aramid substrate is used as an elongated sheet.
Moreover, polyamic acid solution which dissolved polyamic acid in organic solvent is provided to a spinning solution main tank of the electrospinning apparatus(10), and the polyamic acid solution provided to the spinning solution main tank is consecutively and quantitatively provided to a nozzle(2) of a nozzle block(3) provided high voltage through a metering pump. Polyamic acid solution provided from each of the nozzle(2) spun and line-focused on a collector(4) provided high voltage through the nozzle(2), sprayed on the meta-aramid substrate(100), and forms polyamic acid non-woven fabric(200).
In the present invention, for the spinning solution polyamic acid solution is used.
In an embodiment of the present invention, polyamic acid solution is used as spinning solution, but it does not limited thereto.
Here, the meta-aramid substrate(100) of the electrospinning apparatus(10) is carried from a block located in front-end to a block located in rear-end by a supply roller(11) operated by driving of a motor(not shown) and by rotation of an auxiliary belt(6) driving by rotation of the supply roller(11), the process is repeated, and on the meta-aramid substrate(100), polyamic acid nanofiber nonwoven(200) is formed.
In an embodiment of the present invention, instead of an elongated sheet, the meta-aramid substrate(100) is used, but it does not limited thereto.
Therefore, a nanofiber filter laminating formed polyamic acid nanofiber non-woven fabric on the meta-aramid substrate(100) is produced.
Meanwhile, through the electrospinning mentioned as above, by laminating forming polyamic acid nanofiber non-woven fabric on the meta-aramid substrate, forms polyamic acid nanofiber filter.
Polyamic acid nanofiber filter manufactured as mentioned above goes through a laminating device(19), through thermal imidization, and produces polyimide nanofiber filter. The laminating device(19) performs imidization in 150 to 350° C., dehydrates polyamic acid nanofiber non-woven fabric, and produces polyimide nanofiber non-woven fabric(200).
A filter manufacture of the present invention laminating formed polyimide nanofiber on the meta-aramid substrate through the imidization process is completed.
Meanwhile, by differing spinning voltage of a front-end block and a rear-end block of the electrospinning apparatus(10), fiber diameter of nanofiber can be made different. In other words, even though it is the same polyamic acid nanofiber non-woven fabric, when providing low spinning voltage of the front-end block and providing high spinning voltage of the rear-end block, nanofiber with large fiber diameter and polyamic acid nanofiber with small fiber diameter can be laminated consecutively on the meta-aramid substrate(100). For example, when provided low voltage of the front-end block, polyamic acid nanofiber non-woven fabric with thick fiber thickness is formed in the front-end, and when provided high voltage in the rear-end block, polyamic acid nanofiber non-woven fabric with thin fiber thickness can be formed. After electrospinning each of the polyamic acid nanofiber non-woven fabric, and going through imidization, the polyamic acid nanofiber non-woven fabric with thick fiber thickness becomes thick polyimide nanofiber non-woven fabric(300), and on the polyimide nanofiber non-woven fabric(300) with thick fiber thickness, can laminating form polyimide nanofiber non-woven fabric(400) with thin fiber thickness.
In an embodiment of the present invention, by putting a difference in voltage in a front-end block and a rear-end block, a filter consecutively laminating formed polyamic acid nanofiber non-woven fabric with different fiber thickness can be produced.
Here, in order to put a difference in fiber thickness of the polyamic acid nanofiber non-woven fabric(200), the method of differentiating voltage intensity provided to each block(20) of the electrospinning apparatus(10) is used, and other methods such as differentiating concentration of spinning solution, or adjusting space between a nozzle(2) and a collector(4), or adjusting feed speed of an elongated sheet is used.
The following description explains manufacturing method of heat-resistant nanofiber filter electrospinning polyvinylidene fluoride(PVDF) on a cellulose substrate using, and coating ceramic using the electrospinning apparatus.
First, in the present invention, polyvinylidene fluoride is used as polymer of spinning solution, and a cellulose substrate(100) is used as an elongated sheet.
Moreover, polyvinylidene fluoride which dissolved the polyvinylidene fluoride in organic solvent is provided to a spinning solution main tank of the electrospinning apparatus(10). Polyvinylidene fluoride solution provided in the spinning solution main tank is consecutively and quantitatively provided to a plurality of nozzle(2) of a nozzle block(3) provided high voltage through a metering pump. Polyvinylidene fluoride solution provided to each of the nozzle(2) is jetted on the cellulose substrate(100) located on a collector(4) flowing high voltage through the nozzle(2), and forms polyvinylidene fluoride nanofiber non-woven fabric.
Here, in a front-end block(20a) of the electrospinning apparatus(10), the cellulose substrate(100) laminated polyvinylidene fluoride nanofiber is carried from the front-end block(20a) to a rear-end block(20b) by a supply roller(11) operated by a motor(not shown) driving and rotation of an auxiliary belt(6) driving by the supply roller(11) rotation, the process is repeated, and forms polyvinylidene fluoride nanofiber non-woven fabric on the cellulose substrate(100).
Meanwhile, the cellulose substrate(100) has excellent dimensional stability in high temperature and has feature of high heat-resisting property. Fine cellulose fiber has high crystalline and high modulas of elasticity in regard of forming fine porous structure, and essentially in high temperature dimensional stability is very excellent. Because of such feature, cellulose substrate(100) is used in consumer products such as high performance filter, functional paper, sheet for cooking, and air cleaning sheet, and in technical fields such as semiconductor device, board for wiring board, substrate of low linear coefficient of expansion material, and separator for electric condenser such as capacitor.
In an embodiment of the present invention, instead of an elongated sheet, the cellulose substrate(100) is used, but it does not limited thereto.
Here, spinning voltage provided to each block(20) of the electrospinning apparatus(10) is 1 kV or more, and preferably 20 kV or more.
After laminating formed polyvinylidene fluoride nanofiber non-woven fabric(200) on the cellulose substrate(100) through the electrospinning, by producing a ceramic coating film(300) on the polyvinylidene fluoride nanofiber non-woven fabric(200), manufactures a heat-resistance nanofiber filter.
A ceramic coating film is produced by adding inorganic particles and binder resin to acetone on the polyvinylidene fluoride nanofiber non-woven fabric and coating produced slurry.
Inorganic particles comprising the ceramic coating film(300) are SiO2, Al2O3, TiO2, Li3PO4, zeolite, MgO, CaO, BaTiO3, Li2O, LiF, LiOH, Li3N, BaO, Na2O, Li2CO3, CaCO3, LiAlO2, SiO, SnO, SnO2, PbO2, ZnO, P2O5, CuO, MoO, V2O5, B2O3, Si3N4, CeO2, Mn3O4, Sn2P2O, Sn2B2O5, Sn2BPO6, and mixture thereof, especially SiO2 and Al2O3 are preferable.
In addition, the binder is any one or more selected from groups comprising polyvinylidene fluoride(PVDF), polymethyl methacylate(PMMA), polyvinyl alcohol(PVA), and carboxymethyl cellulose(CMS), etc., and it is used in coating and attaching the inorganic particles on the polyvinylidene fluoride nanofiber non-woven fabric.
Also, coating method for forming the ceramic coating film(300) can use various coating methods such as chemical vapor deposition(CVD), physical vapor deposition(PVD), spray coating, dip coating, spin coating, and casting method, and especially coating by casting method is preferable.
Therefore, after laminating formed polyvinylidene fluoride nanofiber non-woven fabric(200) on the cellulose substrate(100), laminating formed the ceramic coating film(300), and a filter of the present invention is produced.
The following description explains exemplary embodiments in detail. It is to be understood that the invention is not limited to the disclosed embodiments, but, on the contrary, is intended to cover various modifications and equivalent arrangements included within the spirit and scope of the appended claims. Exemplary embodiments introduced herein are provided to make disclosed contents thorough and complete to person of ordinary skill in the art.
By dissolving polyamic acid(SANG-A FRONTEC Corp.) in dimethyl acetamide(DMAc) solvent, and producing polyamic acid solution with viscosity of 102,000 cps, and the polyamic acid solution is injected to a spinning solution main tank. In a front-end block provided applied voltage of 15 kV, and electrospinning polyamic acid solution on cellulose substrate with basis weight of 30 gsm, and forms polyamic acid nanofiber non-woven fabric with thickness of 2.5 μm and fiber diameter of 350 nm. In a rear-end block provided applied voltage of 20 kV, and electrospinning the polyamic acid solution on a polyamic nanofiber non-woven fabric with fiber diameter of 350 nm, and forms polyamic acid nanofiber non-woven fabric with thickness of 2.5 μm and fiber diameter of 150 nm. After electrospinning, in a laminating device it goes through heat treatment in 150° C., imidization of polyamic acid, and manufactures a polyimide nanofiber filter. In this case, electrospinning is performed in conditions of the distance between an electrode and a collector is 40 cm, spinning solution flow rate is 0.1 mL/h, temperature 22° C., and humidity 20%.
Except heat treatment performed in 250° C. instead of 150° C., Example 2 performs the same process as Example 1, and manufactures a polyimide nanofiber filter.
Except heat treatment performed in 350° C. instead of 150° C., Example 3 performs the same process as Example 1, and manufactures a polyimide nanofiber filter.
Nylon 6 is dissolved in formic acid and produces nylon 6 solution, and the nylon 6 solution is injected to a spinning solution main tank. By electrospinning on a cellulose substrate on a collector with basis weight of 30 gsm in conditions of applied voltage 20 kV, spinning solution flow rate 0.1 mL/h, temperature 22° C., humidity 20%, and going through a laminating device, nylon 6 nanofiber filter is produced.
By dissolving polyamic acid(SANG-A FRONTEC Corp.) in dimethyl acetamide(DMAc) solvent, and producing polyamic acid solution with concentration of 20 weight % and viscosity of 102,000 cps, and the polyamic acid solution is injected to a spinning solution main tank. In a front-end block provided applied voltage of 15 kV, and electrospinning polyamic acid solution on cellulose substrate with basis weight of 30 gsm, and forms polyamic acid nanofiber non-woven fabric with thickness of 5 μm and fiber diameter of 350 nm. In this case, electrospinning is performed in conditions of the distance between an electrode and a collector is 40 cm, spinning solution flow rate is 0.1 mL/h, temperature 22° C., humidity 20%. After electrospinning, in a laminating device going through heat treatment in 150° C., imidization of polyamic acid, and manufactures a polyimide nanofiber filter.
In example 1 to 3 and comparative example 1 to 2, after cutting each produced filter in 3 cm×3 cm, after stored in 190° for 30 minutes, and evaluated thermal shrinkable rate. The result is in the following Table 1.
In example 1 to 3 and comparative example 1 to 2, in order to measure each produced filter efficiency, DOP test method is used. DOP test method is automation filter analyzer(AFT) of TSI 3160(TSI Incorporated) for measuring efficiency of dioctyl phthalate(DOP), and it can measure permeability of filter medium material, filter efficiency, and differential pressure.
The automation analyzer makes DOP in desired particle size and penetrates it on a filter sheet, and it is a device measuring speed of air, DOP filtering efficiency, air permeability, etc. in coefficient method automatically, and it is a very important device in high efficiency filter.
DOP % Efficiency is Defined as Follows:
DOP % transmissivity=1−100(DOP concentration downstream/DOP concentration upstream)
In exemplary 1 to 3 and comparative example 1 to 2, filtering efficiency of each produced filter is measured according to the method mentioned above, and the result is shown in the following table 2.
As shown in the Table 1 and Table 2, polyimide nanofiber filter manufactured through example 1 to 3 of the present invention is excellent in thermal shrinkable rate and efficiency compared to filter produced in comparative example 1 and 2.
Nanofiber filter each produced in example 1 to 3 and comparative example 1 and 2 measures pressure drop by ASHRAE 52.1 according to flow rate of 50 μg/m3, and measures filter sustainability according to this, and the result is shown in the following Table 3.
According to Table 3, filter produced through example 1 to 3 of the present invention has low pressure drop so less pressure loss, and filter sustainability is longer which results in excellence in durability comparing to filter produced in comparative example 1 and 2.
Polyacrylonitrile(Hanil Synthetic Fiber Co., Ltd.) with weight average molecular weight of 157,000 is dissolved in dimethylformamide and produces polyacrylonitrile solution. The polyacrylonitrile solution is injected to a spinning solution main tank, in a front-end block is provided applied voltage of 15 kV, and in a rear-end block is provided applied voltage of 20 kV and electrospinning on a cellulose substrate with basis weight of 30 gsm. In the front-end block formed polyacrylonitrile nanofiber non-woven fabric with thickness of 2.5 μm and fiber diameter of 350 nm on a cellulose substrate. In a rear-end block laminating formed polyacrylonitrile nanofiber non-woven fabric with thickness of 2.5 μm and fiber diameter of 150 nm on the polyacrylonitrile nanofiber non-woven fabric with thickness of 2.5 μm and fiber diameter of 350 nm, and produces a polyacrylonitrile nanofiber filter. In this case, electrospinning is performed in conditions of the distance between an electrode and a collector is 40 cm, spinning solution flow rate is 0.1 mL/h, temperature 22° C., and humidity 20%.
Polyacrylonitrile(Hanil Synthetic Fiber Co., Ltd.) with weight average molecular weight of 157,000 is dissolved in dimethylformamide and produces polyacrylonitrile solution. The polyacrylonitrile solution is injected to a spinning solution main tank, in a front-end block is provided applied voltage of 15 kV, and in a rear-end block is provided applied voltage of 20 kV and electrospinning on a cellulose substrate. In the front-end block formed polyacrylonitrile nanofiber non-woven fabric with thickness of 3 μm and fiber diameter of 350 nm on a cellulose substrate. In a rear-end block laminating formed polyacrylonitrile nanofiber non-woven fabric with thickness of 2 μm and fiber diameter of 150 nm on the polyacrylonitrile nanofiber non-woven fabric with thickness of 3 μm and fiber diameter of 350 nm, and produces a polyacrylonitrile nanofiber filter. In this case, electrospinning is performed in conditions of the distance between an electrode and a collector is 40 cm, spinning solution flow rate is 0.1 mL/h, temperature 22° C., and humidity 20%.
Polyacrylonitrile(Hanil Synthetic Fiber Co., Ltd.) with weight average molecular weight of 157,000 is dissolved in dimethylformamide and produces polyacrylonitrile solution. The polyacrylonitrile solution is injected to a spinning solution main tank, in a front-end block is provided applied voltage of 15 kV, and in a rear-end block is provided applied voltage of 20 kV and electrospinning on a cellulose substrate. In the front-end block formed polyacrylonitrile nanofiber non-woven fabric with thickness of 2 μm and fiber diameter of 350 nm on a cellulose substrate. In a rear-end block laminating formed polyacrylonitrile nanofiber non-woven fabric with thickness of 3 μm and fiber diameter of 150 nm on the polyacrylonitrile nanofiber non-woven fabric with thickness of 2 μm and fiber diameter of 350 nm, and produces a polyacrylonitrile nanofiber filter. In this case, electrospinning is performed in conditions of the distance between an electrode and a collector is 40 cm, spinning solution flow rate is 0.1 mL/h, temperature 22° C., and humidity 20%.
Except modifying polyacrylonitrile solution in example 4 to polyethersulfone solution dissolved polyethersulfone in dimethylacetamide(DMAc) solvent, Example 7 performs electrospinning in the same condition and manufactures a nanofiber filter.
Except modifying polyacrylonitrile solution in example 5 to polyethersulfone solution dissolved polyethersulfone in dimethylacetamide(DMAc) solvent, Example 8 performs electrospinning in the same condition and manufactures a nanofiber filter.
Except modifying polyacrylonitrile solution in example 6 to polyethersulfone solution dissolved polyethersulfone in dimethylacetamide(DMAc) solvent, Example 9 performs electrospinning in the same condition and manufactures a nanofiber filter.
Nylon 6 solution is manufactured by dissolving nylon 6 in formic acid, and the nylon 6 solution is injected to a spinning solution main tank. In a front-end block provided applied voltage of 15 kV, and electrospinning nylon 46 solution on a cellulose substrate with basis weight of 30 gsm, and forms nylon 6 nanofiber non-woven fabric with thickness of 2.5 μm and fiber diameter of 350 nm. In a rear-end block provided applied voltage of 20 kV, and electrospinning the nylon 6 solution on a nylon 6 non-woven fabric with fiber diameter of 350 nm, and forms nylon 6 nanofiber non-woven fabric with thickness of 2.5 μm and fiber diameter of 150 nm. After electrospinning, in a laminating device, going though heat and pressure treatment, and manufactures a nylon 6 nanofiber filter. In this case, electrospinning is performed in conditions of the distance between an electrode and a collector is 40 cm, spinning solution flow rate is 0.1 mL/h, temperature 22° C., humidity 20%.
Except modifying nylon 6 in example 10 to nylon 46, example 11 performs electrospinning in the same condition, and manufactures a nanofiber filter.
Except modifying nylon 6 in example 10 to nylon 66, example 11 performs electrospinning in the same condition, and manufactures a nanofiber filter.
Nylon 6 solution is manufactured by dissolving nylon 6 in formic acid, and the nylon 6 solution is injected to a spinning solution main tank. In conditions of applied voltage is 20 kV, spinning solution flow rate is 0.1 mL/h, temperature 22° C., humidity 20%, electrospinning on a substrate with basis weight of 30 gsm on a collector, and forms a nylon 6 nanofiber filter with thickness of 5 μm and fiber diameter of 350 nm.
Polyacrylonitrile(Hanil Synthetic Fiber Co., Ltd.) with weight average molecular weight of 157,000 is dissolved in dimethylformamide and produces polyacrylonitrile solution. The polyacrylonitrile solution is injected to a spinning solution main tank, spinning applied voltage is provided 15 kVm electrospinning on a substrate with basis weight of 30 gsm, and forms polyacrylonitrile nanofiber non-woven fabric with thickness of 5 μm and fiber diameter of 350 nm on a cellulose substrate. In this case, electrospinning is performed in conditions of the distance between an electrode and a collector is 40 cm, spinning solution flow rate is 0.1 mL/h, temperature 22° C., and humidity 20%.
Thermal shrinkable rate of nanofiber filter each produced in example 4 to 9 and comparative example 3 and 4 evaluated in the same method as evaluation example 1, and the result is shown in the following table 4.
Filtering efficiency of nanofiber filter each produced in example 4 to 12 and comparative example 3 and 4 evaluated in the same method as evaluation example 2, and the result is shown in the following table 5.
According to the table 4 and table 5, nanofiber filter produced through example 4 to 12 of the present invention has excellent heat-resisting property and filtering efficiency compared to filter produced in example 3 and 4.
Nanofiber filter each produced in example 4 to 12 and comparative example 3 and 4 measured in the same method as example 3, and the result is shown in the following table 6.
According to Table 6, filter produced through example 4 to 12 of the present invention has low pressure drop so less pressure loss, and filter sustainability is longer which results in excellence in durability compared to filter produced in comparative example 3 and 4.
Meta-aramid with viscosity of 50,000 cps and solid content of 20 weight % is dissolved in dimethylacetamide(DMAc) and manufactures meta-aramid solution, and injected to a spinning solution main tank connected to a front-end block. Also, polyamic acid with weight average molecular weight of 100,000 is dissolved in dimethylacetamide(DMAc) solvent and manufactures polyamic acid solution, and injected the polyamic acid solution to a spinning solution main tank connected to a rear-end block. Electrospinning on a cellulose substrate on a collector in electrospinning conditions of the distance between an electrode and a collector is 40 cm, applied voltage is 20 kV, spinning solution flow rate is 0.1 mL/h, temperature 22° C., and humidity 20%. In this case, by electrospinning performed in a front-end block on a cellulose substrate laminating formed meta-aramid nanofiber non-woven fabric with thickness of 2.5 μm, and by electrospinning performed in a rear-end block, laminating formed polyamic acid nanofiber non-woven fabric with thickness of 2.5 μm on meta-aramid nanofiber non-woven fabric. After going through heat treatment in 150° C., imidization of polyamic acid nanofiber non-woven fabric, and produces a meta-aramid/polyimide multi-layered nanofiber filter.
Meta-aramid with viscosity of 50,000 cps and solid content of 20 weight % is dissolved in dimethylacetamide(DMAc) and manufactures meta-aramid solution, and injected to a spinning solution main tank connected to a front-end block. Also, polyamic acid with weight average molecular weight of 100,000 is dissolved in dimethylacetamide(DMAc) solvent and manufactures polyamic acid solution, and injected the polyamic acid solution to a spinning solution main tank connected to a rear-end block. Electrospinning on a cellulose substrate on a collector in electrospinning conditions of the distance between an electrode and a collector is 40 cm, applied voltage is 20 kV, spinning solution flow rate is 0.1 mL/h, temperature 22° C., and humidity 20%. In this case, by electrospinning performed in a front-end block on a cellulose substrate laminating formed meta-aramid nanofiber non-woven fabric with thickness of 3 mm, and by electrospinning performed in a rear-end block, laminating formed polyamic acid nanofiber non-woven fabric with thickness of 2 μm on meta-aramid nanofiber non-woven fabric. After going through heat treatment in 150° C., imidization of polyamic acid nanofiber non-woven fabric, and produces a meta-aramid/polyimide multi-layered nanofiber filter.
Meta-aramid with viscosity of 50,000 cps and solid content of 20 weight % is dissolved in dimethylacetamide(DMAc) and manufactures meta-aramid solution, and injected to a spinning solution main tank connected to a front-end block. Also, polyamic acid with weight average molecular weight of 100,000 is dissolved in dimethylacetamide(DMAc) solvent and manufactures polyamic acid solution, and injected the polyamic acid solution to a spinning solution main tank connected to a rear-end block. Electrospinning on a cellulose substrate on a collector in electrospinning conditions of the distance between an electrode and a collector is 40 cm, applied voltage is 20 kV, spinning solution flow rate is 0.1 mL/h, temperature 22° C., and humidity 20%. In this case, by electrospinning performed in a front-end block on a cellulose substrate laminating formed meta-aramid nanofiber non-woven fabric with thickness of 2 μm, and by electrospinning performed in a rear-end block, laminating formed polyamic acid nanofiber non-woven fabric with thickness of 3 mm on meta-aramid nanofiber non-woven fabric. After going through heat treatment in 150° C., imidization of polyamic acid nanofiber non-woven fabric, and produces a meta-aramid/polyimide multi-layered nanofiber filter.
Polyacrylonitrile(Hanil Synthetic Fiber Co., Ltd.) with weight average molecular weight of 157,000 is dissolved in dimethylformamide(DMF) and produces polyacrylonitrile solution, and the polyacrylonitrile solution is injected to a spinning solution main tank. Also, meta-aramid with viscosity of 50,000 cps and solid content of 20 weight % is dissolved in dimethylacetamide(DMAc) and produces meta-aramid solution, and meta-aramid solution is injected to a spinning solution main tank connected to a rear-end block. Then spinning solution is provided from each spinning solution main tank through nozzle of each block, and electrospinning is performed. In this case, by electrospinning performed in a front-end block laminating formed polyacrylonitrile nanofiber non-woven fabric with thickness of 2.5 μm on a cellulose substrate with basis weight of 30 gsm, and by electrospinning performed in a rear-end block, laminating formed meta-aramid nanofiber non-woven fabric with thickness of 2.5 μm on polyacrylonitrile nanofiber non-woven fabric. In this case, electrospinning is performed in conditions of the distance between an electrode and a collector is 40 cm, applied voltage is 20 kV, spinning solution flow rate is 0.1 mL/h, temperature 22° C., and humidity 20%.
Polyacrylonitrile(Hanil Synthetic Fiber Co., Ltd.) with weight average molecular weight of 157,000 is dissolved in dimethylformamide(DMF) and produces polyacrylonitrile solution, and the polyacrylonitrile solution is injected to a spinning solution main tank. Also, polyamic acid with weight average molecular weight of 100,000 is dissolved in dimethylacetamide(DMAc) solvent and produces polyamic acid solution, and the polyamic acid solution is injected to a spinning solution main tank connected to a rear-end block. Then spinning solution is provided from each spinning solution main tank through nozzle of each block, and electrospinning is performed. In this case, by electrospinning performed in a front-end block laminating formed polyacrylonitrile nanofiber non-woven fabric with thickness of 2.5 μm on a cellulose substrate with basis weight of 30 gsm, and by electrospinning performed in a rear-end block, laminating formed polyamic acid nanofiber non-woven fabric with thickness of 2.5 μm on polyacrylonitrile nanofiber non-woven fabric. Then going through heat-treatment in 150° C., imidization of polyamic acid nanofiber non-woven fabric, and modifies polyamic acid nanofiber non-woven fabric to polyimide nanofiber non-woven fabric. In this case, electrospinning is performed in conditions of the distance between an electrode and a collector is 40 cm, applied voltage is 20 kV, spinning solution flow rate is 0.1 mL/h, temperature 22° C., and humidity 20%.
Polyacrylonitrile(Hanil Synthetic Fiber Co., Ltd.) with weight average molecular weight of 157,000 is dissolved in dimethylformamide(DMF) and produces polyacrylonitrile solution, and the polyacrylonitrile solution is injected to a spinning solution main tank. Also, polyether sulfone with viscosity of 1,200 cps and solid content of 20 weight % is dissolved in dimethylacetamide(DMAc) and produces polyether sulfone solution, and the polyether sulfone solution is injected to a spinning solution main tank connected to a rear-end block. Then spinning solution is provided from each spinning solution main tank through nozzle of each block, and electrospinning is performed. In this case, by electrospinning performed in a front-end block laminating formed polyacrylonitrile nanofiber non-woven fabric with thickness of 2.5 μm on a cellulose substrate with basis weight of 30 gsm, and by electrospinning performed in a rear-end block, laminating formed polyether sulfone nanofiber non-woven fabric with thickness of 2.5 μm on polyacrylonitrile nanofiber non-woven fabric. In this case, electrospinning is performed in conditions of the distance between an electrode and a collector is 40 cm, applied voltage is 20 kV, spinning solution flow rate is 0.1 mL/h, temperature 22° C., and humidity 20%.
By dissolving nylon 6 in formic acid, nylon 6 solution is produced, and the nylon 6 solution is injected to a spinning solution main tank. Electrospinning is performed in conditions of the distance between an electrode and a collector is 40 cm, applied voltage is 20 kV, spinning solution flow rate is 0.1 mL/h, temperature 22° C., and humidity 20%, on a cellulose substrate located on a collector making nanofiber thickness of 5 μm, and going through a laminating device, a nylon 6 nanofiber filter is manufactured.
Meta-aramid with viscosity of 50,000 cps and solid content of 20 weight % is dissolved in dimethylacetamide(DMAc) and manufactures meta-aramid solution. The meta-aramid solution is injected to a spinning solution main tank, after providing spinning applied voltage of 20 kV, electrospinning on a cellulose substrate with basis weight of 30 gsm, and produces a meta-aramid nanofiber filter with thickness of 5 μm. In this case, electrospinning is performed in conditions of the distance between an electrode and a collector is 40 cm, spinning solution flow rate is 0.1 mL/h, temperature 22° C., and humidity 20%.
A cellulose substrate with basis weight of 30 gsm is used as a filter medium.
Except for using polyacrylonitrile solution produced by dissolving polyacrylonitrile solution, which dissolved polyacrylonitrile(Hanil Synthetic Fiber Co., Ltd.) with weight average molecular weight of 157,000 in dimethylformamide(DMF), in dimethyl formamide instead of meta-aramid solution, comparative example 8 performs the same process as comparative example 6, and produces a polyacrylonitrile nanofiber filter.
thermal shrinkable rate of filter each produced in example 13 to 18 and comparative example 5 to 8 is evaluated in the same method as evaluation example 1, and the result is shown in the following table 7.
Filtering efficiency of a filter each produced in example 13 to 18 and comparative example 5 to 8 is evaluated in the same method as evaluation example 2, and the result is shown in the following table 8.
According to the table 7 and table 8, a multi-layered nanofiber filter each produced in example 13 to 18 has excellent thermal shrinkable rate and filtering efficiency compared to a filter each produced in comparative example 5 to 8.
By dissolving polysiloxane(DOW CORNINGMB50-010) having number average molecular weight of 50,000 in acetone solvent and producing polysiloxane solution of 20 weight %, and providing it to a spinning solution main tank of the electrospinning apparatus, in each block, the same polysiloxane solution is provided to a nozzle. After providing applied voltage of 15 kV to a front-end block located in front-end of the block, and in a rear-end block, providing applied voltage of 20 kV, and electrospinning polysiloxane solution on a cellulose substrate with basis weight of 30 gsm. In the front-end block, on the cellulose substrate, polysiloxane nanofiber non-woven fabric with thickness of 2.5 μm and average fiber diameter of 350 nm, and in the rear-end block, on the polysiloxane nanofiber non-woven fabric with fiber diameter of 350 nm, laminating formed polysiloxane nanofiber non-woven fabric with thickness of 2.5 μm and average fiber diameter of 150 nm, and manufactures a polysiloxane nanofiber filter. In this case, the distance between an electrode and a collector is 40 cm, spinning solution flow rate is 0.1 mL/h, temperature 22° C., and humidity 20%.
Except for using a meta-aramid substrate with the same basis weight instead of a cellulose substrate, example 20 performs the same process as example 1, and produces a nanofiber filter.
By dissolving nylon 6 in formic acid, nylon 6 solution is produced, and the nylon 6 solution is injected to a spinning solution main tank. Electrospinning is performed in conditions of applied voltage is 20 kV, spinning solution flow rate is 0.1 mL/h, temperature 22° C., and humidity 20%, on a cellulose substrate with basis weight of 30 gsm located on a collector, and going through a laminating device, a nylon 6 nanofiber filter is manufactured.
By dissolving polysiloxane(DOW CORNINGMB50-010) having number average molecular weight of 50,000 in acetone solvent and producing polysiloxane solution of 20 weight %, and providing it to a spinning solution main tank of the electrospinning apparatus, in each block, the same polysiloxane solution is provided to a nozzle. After providing applied voltage of 15 kV to each of the block, on a cellulose substrate with basis weight of 30 gsm, by electrospinning polysiloxane solution, and laminating formed polysiloxane nanofiber non-woven fabric with thickness of 5 μm and fiber diameter of 350 nm, and manufactures a polysiloxane nanofiber filter.
thermal shrinkable rate of a filter each produced in example 19 and 20 and comparative example 9 and 10 is evaluated in the same method as evaluation example 1, and the result is shown in the following table 9.
Filtering efficiency of a filter each produced in example 19 and 20 and comparative example 9 and 10 is evaluated in the same method as evaluation example 2, and the result is shown in the following table 9.
Pressure drop and filter sustainability of a filter each produced in example 19 and 20 and comparative example 9 and 10 is evaluated in the same method as evaluation example 3, and the result is shown in the following table 10.
According to table 9, filters produced by example 19 and 20 have excellent thermal shrinkable rate compared to a filter produced in comparative example 9, and comparing with comparative example 10, thermal shrinkable rate is similar but filters produced by example 19 and 20 are excellent in terms of filtering efficiency.
Also, according to table 10, filters produced by examples 19 and 20 compared to comparative example 1 and 2 have low pressure drop and longer filter sustainability which result in excellence in durability.
In the first section, polyethersulfone with viscosity of 1,200 cps and solid content of 20 weight % is dissolved in dimethylacetamide(DMAc) and produces polyethersulfone electrospinning solution dope. In the second section, polyamic acid(PAA) with weight average molecular weight of 100,000 is dissolved in mixed solvent(THF/DMAc) of tetrahydrofuran(THF) and dimethylacetamide(DMAc) and produces polyamic acid dope. In electrospinning conditions of the distance between an electrode and a collector is 40 cm, applied voltage is 15 kV, spinning solution flow rate is 0.1 mL/h, temperature 22° C., and humidity 20%, forming polyethersulfone nanofiber with thickness of 3 μm on a meta-aramid substrate with basis weight of 30 gsm, a collector moves in predetermined speed, spinning polyamic acid nanofiber making thickness of 3 μm on polyethersulfone nanofiber layer, and after forming nanofiber layer, by heating in 200° C., imdization of polyamic acid nanofiber to polyimide nanofiber, and forms a multi-layered filter medium.
In the first section, polyethersulfone with viscosity of 1,200 cps and solid content of 20 weight % is dissolved in dimethylacetamide(DMAc) and produces polyethersulfone electrospinning solution dope. In the second section, polyamic acid(PAA) with weight average molecular weight of 100,000 is dissolved in mixed solvent(THF/DMAc) of tetrahydrofuran(THF) and dimethylacetamide(DMAc) and produces polyamic acid dope. In electrospinning conditions of the distance between an electrode and a collector is 40 cm, applied voltage is 15 kV, spinning solution flow rate is 0.1 mL/h, temperature 22° C., and humidity 20%, forming polyethersulfone nanofiber with thickness of 1 μm on a meta-aramid substrate with basis weight of 30 gsm, a collector moves in predetermined speed, spinning polyamic acid nanofiber making thickness of 5 μm on polyethersulfone nanofiber layer, and after forming nanofiber layer, by heating in 200° C., imdization of polyamic acid nanofiber to polyimide nanofiber, and forms a multi-layered filter medium.
Except for making polyethersulfone nanofiber thickness to 5 μm and polyamic acid nanofiber thickness to 1 μm, example 23 performs the same process as example 21, and produces a multi-layered filter medium.
In the first section, polyethersulfone with viscosity of 1,200 cps and solid content of 20 weight % is dissolved in dimethylacetamide(DMAc) and produces polyethersulfone electrospinning solution dope. In the second section, polyamic acid(PAA) with weight average molecular weight of 100,000 is dissolved in mixed solvent(THF/DMAc) of tetrahydrofuran(THF) and dimethylacetamide(DMAc) and produces polyamic acid dope. In electrospinning conditions of the distance between an electrode and a collector is 40 cm, spinning solution flow rate is 0.1 mL/h, temperature 22° C., and humidity 20%, forming polyethersulfone nanofiber with thickness of 3 μm on a meta-aramid substrate with basis weight of 30 gsm, forming nanofiber with fiber diameter of 400 nm, a collector moves in predetermined speed, in the second section spinning polyamic acid nanofiber making thickness of 3 μm on polyethersulfone nanofiber layer in applied voltage of 20 kV, and after forming nanofiber layer with fiber diameter of 100 nm, by heating in 200° C., imdization of polyamic acid nanofiber to polyimide nanofiber, and forms a multi-layered filter medium.
In the first section, polyethersulfone with viscosity of 1,200 cps and solid content of 20 weight % is dissolved in dimethylacetamide(DMAc) and produces polyethersulfone electrospinning solution dope. In the second section, polyamic acid(PAA) with weight average molecular weight of 100,000 is dissolved in mixed solvent(THF/DMAc) of tetrahydrofuran(THF) and dimethylacetamide(DMAc) and produces polyamic acid dope. In electrospinning conditions of the distance between an electrode and a collector is 40 cm, spinning solution flow rate is 0.1 mL/h, temperature 22° C., and humidity 20%, forming polyethersulfone nanofiber with thickness of 3 μm on a meta-aramid substrate with basis weight of 30 gsm, forming nanofiber with fiber diameter of 100 nm in applied voltage of 20 kV, a collector moves in predetermined speed, in the second section spinning polyamic acid nanofiber making thickness of 3 μm on polyethersulfone nanofiber layer in applied voltage of 12 kV, and after forming nanofiber layer with fiber diameter of 400 nm, by heating in 200° C., imdization of polyamic acid nanofiber to polyimide nanofiber, and forms a multi-layered filter medium.
In the first section, meta-aramid with viscosity of 50,000 cps and solid content of 20 weight % is dissolved in dimethylacetamide(DMAc) and produces meta-aramid electrospinning solution dope. In the second section, polyamic acid(PAA) with weight average molecular weight of 100,000 is dissolved in mixed solvent(THF/DMAc) of tetrahydrofuran(THF) and dimethylacetamide(DMAc) and produces polyamic acid dope. In electrospinning conditions of the distance between an electrode and a collector is 40 cm, applied voltage is 15 kV, spinning solution flow rate is 0.1 mL/h, temperature 22° C., and humidity 20%, forming meta-aramid nanofiber with thickness of 3 μm on a meta-aramid substrate with basis weight of 30 gsm, a collector moves in predetermined speed, in the second section spinning polyamic acid nanofiber making thickness of 3 μm on meta-aramid nanofiber layer, and after forming nanofiber layer, by heating in 200° C., imdization of polyamic acid nanofiber to polyimide nanofiber, and forms a multi-layered filter medium.
Except for using meta-aramid of 10 weight % instead of solid content of 20 weight %, meta-aramid nanofiber thickness is 1 μm, and polyamic acid nanofiber thickness is 5 μm, example 27 performs the same process as example 26, and manufactures a multi-layered filter medium.
Except for making meta-aramid nanofiber thickness to 5 μm and polyamic acid nanofiber thickness to 1 μm, example 28 performs the same process as example 26, and produces a multi-layered filter medium.
Except for forming meta-aramid nanofiber with fiber diameter of 400 nm on a meta-aramid substrate, and forming polyamic acid nanofiber with fiber thickness of 100 nm on a meta-aramid nanofiber layer, example 29 performs the same process as example 26, and produces a multi-layered filter medium.
Except for forming meta-aramid nanofiber with fiber diameter of 100 nm on a meta-aramid substrate, and forming polyamic acid nanofiber with fiber thickness of 400 nm on a meta-aramid nanofiber layer, example 30 performs the same process as example 26, and produces a multi-layered filter medium.
In the first section, polyamic acid(PAA) with weight average molecular weight of 100,000 is dissolved in mixed solvent(THF/DMAc) of tetrahydrofuran(THF) and dimethylacetamide(DMAc) and produces polyamic acid dope. In the second section, polysiloxane(DOW CORNINGMB50-010), which is among one of inorganic polymer and number average molecular weight is 50,000, is dissolved in acetone solvent and produces polysiloxane dope of 20 weight %. In electrospinning conditions of the distance between an electrode and a collector is 40 cm, applied voltage is 15 kV, spinning solution flow rate is 0.1 mL/h, temperature 22° C., and humidity 20%, forming polyamic acid nanofiber with thickness of 3 μm on a meta-aramid substrate with basis weight of 30 gsm, a collector moves in predetermined speed, and in the second section, spinning polyamic acid nanofiber making thickness of 3 μm on polyamic acid nanofiber laminated side and forming nanofiber layer, by heating in 200° C., imdization of polyamic acid nanofiber to polyimide nanofiber, and forms a multi-layered filter medium.
Except for using meta-aramid dope produced by dissolving meta-aramid with viscosity of 50,000 cps and solid content of 20 weight % in dimethylacetamide(DMAc) instead of polyamic acid dope in the first section, example 32 performs the same process as example 31, and manufactures a filter medium.
Except for using spinning solution produced by dissolving polyacrylonitrile(Hanil Synthetic) with weight average molecular weight of 157,000 in dimethylformamide(DMF) instead of polyamic acid dope in the first section, example 33 performs the same process as example 31, and manufactures a filter medium.
Except for using spinning solution produced by dissolving polyvinylidene fluoride(KYNAR 741) with weight average molecular weight of 500,000 in dimethylacetamide(DMAc) solvent instead of polyamic acid dope in the first section, example 34 performs the same process as example 31, and manufactures a filter medium.
Except for using polymer spinning solution by dissolving nylon 6 homopolymer which is one kind of polyamide in solvent with weight ratio of 5:5 in tetrafluoro acetic acid(TFA) and dichloromethane(DCM) instead of polyamic acid dope in the first section, example 35 performs the same process as example 31, and produces a filter medium.
Except for using polyether sulfone dope produced by dissolving polyether sulfone with viscosity of 1,200 cps and solid content of 20 weight % in dimethylacetamide(DMAc), example 36 performs the same process as example 31, and produces a filter medium.
By dissolving polyether sulfone with viscosity of 1,200 cps and solid content of 20 weight % in dimethylacetamide(DMAc) and produces polyether sulfone dope. In electrospinning conditions of the distance between an electrode and a collector is 40 cm, applied voltage is 15 kV, spinning solution flow rate is 0.1 mL/h, temperature 22° C., and humidity 20%, forming polyether sulfone nanofiber with thickness of 6 μm on a meta-aramid substrate with basis weight of 30 gsm, and forms a filter medium.
Except for using meta-aramid dope dissolving meta-aramid with viscosity of 50,000 cps and solid content of 20 weight % in dimethylacetamide(DMAc) instead of polyether sulfone dope, comparative example 12 performs the same process as comparative example 11, and manufactures a filter medium.
A filter each produced in example 21 to 36 and comparative example 11 and 12 is heated and pressured in nip pressure of 50 kg/cm in temperature of 200° C. measures fiber contraction, and evaluates heat-resisting property, and the result is shown in the following table 11.
Filtering efficiency of filter each produced in example 21 to 36 and comparative example 11 and 12 is measured in the same method as evaluation example 2, and the result is shown in the following table 12.
According to the table 11 and table 12, a multi-layered nanofiber filter each produced in example 21 to 36 has excellent fiber contraction rate and filtering efficiency compared to a filter produced each in comparative example 11 and 12.
Nylon 6 solution is manufactured by dissolving nylon 6 in formic acid, and the nylon 6 solution is injected to a spinning solution main tank. In a front-end block provided applied voltage of 15 kV, and electrospinning nylon 46 solution on a bicomponent substrate with basis weight of 30 gsm, and laminating formed nylon 6 nanofiber non-woven fabric with thickness of 2.5 μm and fiber diameter of 350 nm. In a rear-end block provided applied voltage of 20 kV, and electrospinning the nylon 6 solution on a nylon 6 non-woven fabric with fiber diameter of 350 nm, and forms nylon 6 nanofiber non-woven fabric with thickness of 2.5 μm and fiber diameter of 150 nm.
After electrospinning, in a laminating device, going though heat and pressure treatment, and manufacturing a filter comprising nylon 6 nanofiber non-woven fabric and a bicomponent substrate. In this case, electrospinning is performed in conditions of the distance between an electrode and a collector is 40 cm, spinning solution flow rate is 0.1 mL/h, temperature 22° C., and humidity 20%.
Except for using nylon 46 instead of nylon 6, example 38 performs the same process as example 37, and produces a filter.
Except for using nylon 66 instead of nylon 6, example 39 performs the same process as example 37, and produces a filter.
Polyvinylidene fluoride of weight average molecular weight of 50,000 is dissolved in dimethyl acetamide and produces polyvinylidene fluoride solution, and the polyvinylidene fluoride solution is injected to a spinning solution main tank. In a front-end block, applied voltage is provided 15 kV, and electrospinning polyvinylidene fluoride solution on a bicomponent substrate with basis weight of 30 gsm, and laminating formed polyvinylidene fluoride nanofiber non-woven fabric having thickness of 2.5 μm and fiber diameter of 350 nm. In a rear-end block, applied voltage is provided 20 kV, and the polyvinylidene fluoride solution used in the front-end electrospins on the polyvinylidene fluoride nanofiber non-woven fabric with fiber diameter of 350, and laminating formed polyvinylidene fluoride nanofiber non-woven fabric with thickness of 2.5 μm and fiber diameter of 150 nm. After electrospinning, in a laminating device heated and pressed, and finally producing a filter comprising polyvinylidene fluoride nanofiber non-woven fabric and a bicomponent substrate. In this case, electrospinning is performed in conditions of the distance between an electrode and a collector is 40 cm, spinning solution flow rate is 0.1 mL/h, temperature 22° C., and humidity 20%.
Polyvinylidene fluoride with weight average molecular weight of 50,000 is dissolved in dimethyl acetamide and produces polyvinylidene fluoride solution, and the polyvinylidene fluoride solution is injected to a spinning solution main tank. In a front-end block, applied voltage is provided 15 kV, and electrospinning polyvinylidene fluoride solution on a bicomponent substrate with basis weight of 30 gsm, and laminating formed polyvinylidene fluoride nanofiber non-woven fabric having thickness of 3 μm and fiber diameter of 350 nm. In a rear-end block, applied voltage is provided 20 kV, and the polyvinylidene fluoride solution used in the front-end electrospins on the polyvinylidene fluoride nanofiber non-woven fabric with fiber diameter of 350, and laminating formed polyvinylidene fluoride nanofiber non-woven fabric with thickness of 2 μm and fiber diameter of 150 nm. After electrospinning, in a laminating device heated and pressed, and finally producing a filter comprising polyvinylidene fluoride nanofiber non-woven fabric and a bicomponent substrate. In this case, electrospinning is performed in conditions of the distance between an electrode and a collector is 40 cm, spinning solution flow rate is 0.1 mL/h, temperature 22° C., and humidity 20%.
Polyvinylidene fluoride with weight average molecular weight of 50,000 is dissolved in dimethyl acetamide and produces polyvinylidene fluoride solution, and the polyvinylidene fluoride solution is injected to a spinning solution main tank. In a front-end block, applied voltage is provided 15 kV, and electrospinning polyvinylidene fluoride solution on a bicomponent substrate with basis weight of 30 gsm, and laminating formed polyvinylidene fluoride nanofiber non-woven fabric having thickness of 2 μm and fiber diameter of 350 nm. In a rear-end block, applied voltage is provided 20 kV, and the polyvinylidene fluoride solution used in the front-end electrospins on the polyvinylidene fluoride nanofiber non-woven fabric with fiber diameter of 350, and laminating formed polyvinylidene fluoride nanofiber non-woven fabric with thickness of 3 μm and fiber diameter of 150 nm. After electrospinning, in a laminating device heated and pressed, and finally producing a filter comprising polyvinylidene fluoride nanofiber non-woven fabric and a bicomponent substrate. In this case, electrospinning is performed in conditions of the distance between an electrode and a collector is 40 cm, spinning solution flow rate is 0.1 mL/h, temperature 22° C., and humidity 20%.
Nylon 6 solution is manufactured by dissolving nylon 6 in formic acid, and the nylon 6 solution is injected to a spinning solution main tank. In conditions of applied voltage 15 kV, spinning solution flow rate is 0.1 mL/h, temperature 22° C., and humidity 20%, on a bicomponent substrate located on a collector, electrospinning is performed making thickness of 5 μm and fiber diameter of 350 nm, and going through a laminating device, a nylon 6 nanofiber filter is produced.
Except for using polyvinylidene fluoride solution produced by dissolving polyvinylidene fluoride with weight average molecular weight of 50,000 in dimethyl acetamide instead of nylon 6 solution, comparative example performs the same process as comparative example 13 and produces a filter.
Filtering efficiency of filter each produced in example 37 to 42 and comparative example 13 and 14 is measured the same method as evaluation example 2, and the result is shown in the following table 13.
Pressure drop and sustainability of filter each produced in example 37 to example 42 and comparative example 13 and 14 is measured the same method as evaluation example 3, and the result is shown in the following table 14.
According to table 13 and table 14, a filter each produced in example 37 to example 42 compared to a filter each produced in comparative example 13 and 14 has excellent filtering efficiency and has low pressure drop which results in less pressure lose, and longer filter sustainability which results in excellence in durability.
Polyacrylonitrile(Hanil Synthetic Fiber Co., Ltd.) with weight average molecular weight of 157,000 is dissolved in dimethylformamide(DMF) and produces polyacrylonitrile solution. The polyacrylonitrile solution is injected to a spinning solution main tank which is connected to a front-end block. Also, meta-aramid with viscosity of 50,000 cps and solid content of 20 weight % is dissolved in dimethylacetamide(DMAc) and produces meta-aramid solution, and the meta-aramid solution is injected to a spinning solution main tank connected to a middle block. Moreover, polyamic acid with weight average molecular weight of 100,000 is dissolved in dimethylacetamide(DMAc) solvent and produces polyamic acid solution, and the polyamic acid solution is injected to a spinning solution main tank connected to a rear-end block. Then spinning solution is provided from each spinning solution main tank through nozzle of each block, and electrospinning is performed. In this case, by electrospinning performed in a front-end block laminating formed polyacrylonitrile nanofiber non-woven fabric with thickness of 2 μm on a cellulose substrate with basis weight of 30 gsm, by electrospinning performed in a middle block, laminating formed meta-aramid nanofiber non-woven fabric with thickness of 2 μm on the polyacrylonitrile nanofiber non-woven fabric, and by electrospinning performed in a rear-end block, laminating formed polyamic acid nanofiber non-woven fabric with thickness of 2 μm on the meta-aramid nanofiber non-woven fabric. Then going through heat treatment in 150° C., imidization of polyamic acid nanofiber non-woven fabric, and modifying polyamic acid nanofiber non-woven fabric to polyimide nanofiber non-woven fabric. Electrospinning is performed in conditions of the distance between an electrode and a collector is 40 cm, applied voltage is 20 kV, spinning solution flow rate is 0.1 mL/h, temperature 22° C., and humidity 20%.
Except for forming thickness of polyacrylonitrile nanofiber non-woven fabric to 3 μm and thickness of polyamic acid nanofiber non-woven fabric to mm, example 44 performs the same process as example 43, and produces a nanofiber filter.
Except for forming thickness of polyacrylonitrile nanofiber non-woven fabric to 1 μm and thickness of polyamic acid nanofiber non-woven fabric to 3 μm, example 45 performs the same process as example 43, and produces a nanofiber filter.
By using cellulose substrate with basis weight of 30 gsm and produces a filter medium.
Polyacrylonitrile(Hanil Synthetic Fiber Co., Ltd.) with weight average molecular weight of 157,000 is dissolved in dimethylformamide(DMF) and produces polyacrylonitrile solution. The polyacrylonitrile solution is injected to a spinning solution main tank, after providing spinning applied voltage of 20 kV, electrospinning on a cellulose substrate with basis weight of 30 gsm, and produces a polyacrylonitrile nanofiber filter with thickness of 6 μm. In this case, electrospinning is performed in conditions of the distance between an electrode and a collector is 40 cm, spinning solution flow rate is 0.1 mL/h, temperature 22° C., and humidity 20%.
Thermal shrinkable rate of filter each produced in example 43 to 45 and comparative example 15 and 16 is evaluated the same method as evaluation example 1, and the result is shown in the following table 15.
Filtering efficiency of filter each produced in example 43 to 45 and comparative example 15 and 16 is measured the same method as evaluation example 2, and the result is shown in the following example 16.
According to the table 15 and table 16, a nanofiber filter each produced in example 42 to 45 compared to a filter each produced in comparative example 15 and 16 has excellent thermal shrinkable rate and excellent filtering efficiency.
In the first section, polyvinylidene fluoride(KYNAR 741) with weight average molecular weight of 500,000 is dissolved in dimethylacetamide(DMAc) solvent and produces spinning solution, and in the second section, polyacrylonitrile(Hanil Synthetic) with weight average molecular weight of 157,000 is dissolved in dimethylformamide(DMF) and produces spinning solution. In the first section, in electrospinning conditions of the distance between an electrode and a collector is 40 cm, applied voltage is 15 kV, spinning solution flow rate is 0.1 mL/h, temperature 22° C., and humidity 20%, forming polyvinylidene fluoride nanofiber with thickness of 31 μm and average diameter of 500 nm on a meta-aramid substrate with basis weight of 30 gsm, and a collector is moved in predetermined speed, in the second section, after laminating polyacrylonitrile nanofiber making thickness of 3 μm and average diameter of 200 nm, laminating a cellulose substrate with basis weight of 30 gsm on polyacrylonitrile nanofiber layer, and forms a filter medium formed nanofiber layer between substrates.
In the first section, meta-aramid with viscosity of 50,000 cps and solid content of 20 weight % is dissolved in dimethylacetamide(DMAc) and produces meta-aramid spinning solution, and in the second section, polyamic acid(PAA) with weight average molecular weight of 100,000 is dissolved in mixed solvent(THF/DMAc) of tetrahydrofuran(THF) and dimethylacetamide(DMAc), and produces polyamic acid dope. In the first section, in electrospinning conditions of the distance between an electrode and a collector is 40 cm, applied voltage is 15 kV, spinning solution flow rate is 0.1 mL/h, temperature 22° C., and humidity 20%, forming meta-aramid nanofiber with thickness of 3 μm and average diameter of 500 nm on a cellulose substrate with basis weight of 30 gsm, and a collector is moved in predetermined speed, in the second section, after laminating precursor(polyamic acid) nanofiber making thickness of 3 μm and average diameter of 200 nm, laminating a meta-aramid substrate with basis weight of 30 gsm on polyamic acid nanofiber layer, in order to imidization of polyamic acid nanofiber layer, in 200° C. heating and laminating, and forms a filter medium formed nanofiber layer between substrates.
In the first section, meta-aramid with viscosity of 50,000 cps and solid content of 20 weight % is dissolved in dimethylacetamide(DMAc) and produces meta-aramid spinning solution, and in the second section, polyacrylonitrile(Hanil Synthetic) with weight average molecular weight of 157,000 is dissolved in dimethylformamide(DMF) and produces spinning solution. In the first section, in electrospinning conditions of the distance between an electrode and a collector is 40 cm, applied voltage is 15 kV, spinning solution flow rate is 0.1 mL/h, temperature 22° C., and humidity 20%, forming meta-aramid nanofiber with thickness of 3 μm and average diameter of 500 nm on a meta-aramid substrate with basis weight of 30 gsm, and a collector is moved in predetermined speed, in the second section, after laminating polyacrylonitrile nanofiber making thickness of 3 μm and average diameter of 200 nm, laminating a cellulose substrate with basis weight of 30 gsm on polyacrylonitrile nanofiber layer, and forms a filter medium formed nanofiber layer between substrates.
In the first section, polyvinylidene fluoride(KYNAR 741) with weight average molecular weight of 500,000 is dissolved in dimethylacetamide(DMAc) solvent and produces spinning solution, and in the second section, polyamic acid(PAA) with weight average molecular weight of 100,000 is dissolved in mixed solvent(THF/DMAc) of tetrahydrofuran(THF) and dimethylacetamide(DMAc). In the first section, in electrospinning conditions of the distance between an electrode and a collector is 40 cm, applied voltage is 15 kV, spinning solution flow rate is 0.1 mL/h, temperature 22° C., and humidity 20%, forming polyvinylidene fluoride nanofiber with thickness of 3 μm and average diameter of 500 nm on a cellulose substrate with basis weight of 30 gsm, and a collector is moved in predetermined speed, in the second section, after laminating polyimide precursor(polyamic acid) nanofiber making thickness of 3 μm and average diameter of 200 nm, in order to put a meta-aramid substrate with basis weight of 30 gsm on polyamic acid nanofiber layer, and imidization of polyamic acid nanofiber layer, in 200° C. heating and laminating, and forms a filter medium formed nanofiber layer between substrates.
In the first section, nylon 6 homopolymer which is one kind of polyamide is dissolved in solvent which has weight ratio 5:5 of tetrafluoroaceticacid(TFA) and dichloromethane(DCM) and produces spinning solution, and in the second section, polyethersulfone with viscosity of 1,200 cps and solid content of 20 weight % is dissolved in dimethylacetamide(DMAc), and produces polyethersulfone dope. In the first section, in electrospinning conditions of the distance between an electrode and a collector is 40 cm, applied voltage is 15 kV, spinning solution flow rate is 0.1 mL/h, temperature 22° C., and humidity 20%, forming polyamide nanofiber with thickness of 3 μm and average diameter of 500 nm on a cellulose substrate with basis weight of 30 gsm, and a collector is moved in predetermined speed, in the second section, after laminating polyethersulfone nanofiber making thickness of 3 μm and average diameter of 200 nm, putting a meta-aramid substrate with basis weight of 30 gsm on polyethersulfone nanofiber layer, and laminating, and forms a filter medium formed nanofiber layer between substrates.
Meta-aramid with viscosity of 50,000 cps and solid content of 20 weight % is dissolved in dimethylacetamide(DMAc) and produces meta-aramid dope. In electrospinning conditions of the distance between an electrode and a collector is 40 cm, applied voltage is 15 kV, spinning solution flow rate is 0.1 mL/h, temperature 22° C., and humidity 20%, laminating meta-aramid nanofiber with thickness of 6 μm on a cellulose substrate with basis weight of 30 gsm, and forms a filter medium.
Thermal shrinkable rate of filter each produced in example 46 to 50 and comparative example 17 is evaluated the same method as evaluation example 1, and the result is shown in the following table 17.
Filtering efficiency of filter each produced in example 46 to 50 and comparative example 17 is evaluated the same method as evaluation example 2, and the result is shown in the following table 17.
According to the table 17, a filter each produced in example 46 to 50 compared to a filter produced in comparative example 17 has excellent thermal shrinkable rate and filtering efficiency.
Polyethersulfone with viscosity of 1,200 cps and solid content of 20 weight % is dissolved in dimethyl formamide and produces spinning solution, and the spinning solution electrospins on a meta-aramid substrate in conditions of the distance between an electrode and a collector is 40 cm, applied voltage 20 kV, spinning solution flow rate is 0.1 mL/h, temperature 22° C., and humidity 20%, laminating formed polyethersulfone nanofiber non-woven fabric with thickness of 5 μm, and produces a filter.
Polyethersulfone with viscosity of 1,200 cps and solid content of 20 weight % is dissolved in dimethyl formamide and produces polyethersulfone solution, and the polyethersulfone solution is injected to a spinning solution main tank. In a front-end block, after providing applied voltage of 15 kV, electrospinning polyethersulfone solution on a meta-aramid substrate with basis weight of 30 gsm, and laminating formed polyethersulfone nanofiber non-woven fabric with thickness of 2.5 μm and fiber diameter of 350 nm. In a rear-end block, after providing applied voltage of 20 kV, electrospinning polyethersulfone solution on the polyethersulfone nanofiber non-woven fabric, laminating formed polyethersulfone nanofiber non-woven fabric with thickness of 2.5 μm and fiber diameter of 150 nm, and produces a filter. In this case, electrospinning is performed in conditions of the distance between an electrode and a collector is 40 cm, spinning solution flow rate is 0.1 mL/h, temperature 22° C., and humidity 20%.
Polyamic acid with weight average molecular weight of 100,000 is dissolved in dimethylacetamide(DMAc) and produces spinning solution, and the spinning solution electrospins on a meta-aramid substrate with basis weight of 30 gsm in conditions of the distance between an electrode and a collector is 40 cm, applied voltage is 20 kV, spinning solution flow rate is 0.1 mL/h, temperature 22° C., and humidity 20%, laminating formed polyamic acid nanofiber non-woven fabric with thickness of 5 μm. Then in a laminating device, performing heat treatment in 150° C., imdization of polyamic acid, and produces a polyimide nanofiber filter.
Except for performing heat treatment in a laminating device in 250° C. instead of 150° C., example 54 performs the same process as example 53, and produces a nanofiber filter.
Except for performing heat treatment in a laminating device in 350° C. instead of 150° C., example 55 performs the same process as example 53, and produces a nanofiber filter.
Polyamic acid of weight average molecular weight of 100,000 is dissolved in dimethyl acetamide(DMAc) and produces polyamic acid solution, and the polyamic acid solution is injected to a spinning solution main tank which provides spinning solution to each block of the electrospinning apparatus. In a front-end block located in front-end, applied voltage is provided 15 kV, and electrospinning polyamic acid solution on a meta-aramid substrate with basis weight of 30 gsm, and laminating formed polyamic acid nanofiber non-woven fabric having thickness of 2.5 μm and fiber diameter of 350 nm. In a rear-end block located in rear-end, applied voltage is provided 20 kV, and polyamic acid solution electrospins on the polyamic acid nanofiber non-woven fabric, and laminating formed polyamic acid nanofiber non-woven fabric with thickness of 2.5 μm and fiber diameter of 150 nm, and produces a filter. In this case, electrospinning is performed in conditions of the distance between an electrode and a collector is 40 cm, spinning solution flow rate is 0.1 mL/h, temperature 22° C., and humidity 20%. Then in a laminating device, performing heat treatment in 150° C., imdization of polyamic acid nanofiber non-woven fabric, and produces a polyimide nanofiber filter.
By using a meta-aramid substrate, produces a filter medium.
Except for using a polyethylene terephthalate(PET) substrate instead of a meta-aramid substrate, comparative example 19 performs the same process as example 51, and produces a nanofiber filter.
A filter each produced in example 51 to 56 and comparative example 18 and 19 is cut in size of 5 cm×2.5 cm, put them between two pieces of slide glass and tighten with a clip, and after leaving in 150° C. for 30 minutes, measures contraction rate, and the result is shown in the following table 18.
A filter each produced in example 51 to 56 and comparative example 18 and 19 is evaluated in the same method as evaluation example 2, and the result is shown in the following table 18.
A nanofiber filter each produced in example 51 to 56 compared to a filter(comparative example 18) produced only using a meata-aramid substrate has excellent filtering efficiency. Also, a nanofiber filter each produced in example 51 to 56 and a nanofiber filter produced in comparative example 19 have polyethersulfone nanofiber non-woven fabric and are similar in filtering efficiency, but a nanofiber filter which used a meta-aramid substrate in example 51 to 56 has far better thermal shrinkable rate.
Polyvinylidene fluoride with weight average molecular weight of 50,000 is dissolved in N-Dimethylacetamide(DMAc) and produces spinning solution, and the spinning solution electrospins on a cellulose substrate with basis weight of 30 gsm in conditions of the distance between an electrode and a collector is 40 cm, applied voltage is 20 kV, spinning solution flow rate is 0.1 mL/h, temperature 22° C., and humidity 20%, laminating formed polyvinylidene fluoride nanofiber non-woven fabric with thickness of 3 μm. Then slurry produced by adding acetone in weight ratio of 9:1 in Al2O3 inorganic particle in size of 0.5 μm and polymethyl metacrylate(PMMA)(LG IG840) which is binder, casting on nanofiber non-woven fabric in thickness of 2 μm.
Except for modifying weight ratio of 9:1 in Al2O3 inorganic particle in size of 0.5 μm and polymethyl metacrylate(PMMA) (LG IG840) which is binder to 8:2 weight ratio, example 58 performs the same process as example 57, and produces a nanofiber filter.
Nylon 6 is dissolved in formic acid and produces nylon 6 solution, and the nylon 6 solution is injected to a spinning solution main tank. By electrospinning in thickness of 5 μm in conditions of applied voltage 20 kV, spinning solution flow rate 0.1 mL/h, temperature 22° C., humidity 20%, on a cellulose substrate with basis weight of 30 gsm on a collector, and produces a nylon 6 nanofiber filter.
By only using polyethylene terephthalate, a filter medium is produced.
A filter each produced in example 57 and 58 and comparative example 20 is cut in size of 5 cm×2.5 cm, put them between two pieces of slide glass and tighten with a clip, and after leaving in 150° for 30 minutes, measures contraction rate, and the result is shown in the following table 19.
Filtering efficiency of a filter each produced in example 57 and 58 and comparative example 21 is evaluated in the same method as evaluation example 2, and the result is shown in the following table 20.
According to the table 19 and table 20, a nanofiber filter each produced in example 57 and 58 compared to a filter produced in comparative example 20 has lower thermal shrinkable rate and excellent heat-resistant stability, and compared to a filter produced in comparative example 21 has far better filtering efficiency.
| Number | Date | Country | Kind |
|---|---|---|---|
| 10-2013-0091638 | Aug 2013 | KR | national |
| 10-2013-0091639 | Aug 2013 | KR | national |
| 10-2013-0091640 | Aug 2013 | KR | national |
| 10-2013-0091641 | Aug 2013 | KR | national |
| 10-2013-0091643 | Aug 2013 | KR | national |
| 10-2013-0091644 | Aug 2013 | KR | national |
| 10-2013-0091645 | Aug 2013 | KR | national |
| 10-2013-0091647 | Aug 2013 | KR | national |
| 10-2013-0091648 | Aug 2013 | KR | national |
| 10-2013-0091649 | Aug 2013 | KR | national |
| 10-2013-0091650 | Aug 2013 | KR | national |
| 10-2013-0091651 | Aug 2013 | KR | national |
| 10-2013-0091652 | Aug 2013 | KR | national |
| 10-2013-0091653 | Aug 2013 | KR | national |
| 10-2013-0091660 | Aug 2013 | KR | national |
| 10-2013-0091661 | Aug 2013 | KR | national |
| Filing Document | Filing Date | Country | Kind |
|---|---|---|---|
| PCT/KR2014/001569 | 2/26/2014 | WO | 00 |
