KR101834400B1 - Nanofiber web with excellent adhesion, a separator using it and its method - Google Patents

Abstract

The present invention relates to a first thermoplastic polyurethane base; A first nanofiber having a basis weight of 0.1 to 2 g / m < 2 > formed by electrospinning a first polymer spinning solution on the first thermoplastic polyurethane base; A second nanofiber having a basis weight of 0.1 to 2 g / m < 2 > formed by electrospinning a second polymer spinning solution on the first nanofiber; And a second thermoplastic polyurethane substrate laminated on the second nanofibers, wherein the nanofiber filter has improved adhesion.
The nanofiber filter according to the present invention is advantageous in that it can be partially melted in a high-temperature laminating environment due to its thermoplastic property and can be used as an adhesive without a separate adhesive by using a thermoplastic polyurethane nonwoven fabric as a base material. Further, by forming the nanofibers on the substrate in a laminated form, the heat resistance is further improved and the filtering efficiency of the filter is excellent. In addition, an electrospinning device for spinning nanofibers is provided with several blocks, so that mass production of nanofibers is possible.

Description

[0001] The present invention relates to a nanofiber web having improved adhesion, a separator using the same, and a method for manufacturing the same,

The present invention relates to a nanofiber web having improved adhesion and a separation membrane using the same and, more particularly, to a nanofiber web in which two or more layers of nanofibers are formed between thermoplastic polyurethane bases to improve adhesion, .

Generally, a gas turbine used in a thermal power plant sucks and compresses purified air from the outside, injects compressed air into the combustor together with the fuel, mixes the mixed air and fuel, And then the high-temperature and high-pressure combustion gas is injected into the vanes of the turbine to obtain a rotational force.

Since these gas turbines are made up of very precise parts, they are subjected to periodic planned preventive maintenance and air filters are used for the pretreatment to purify the air in the compressor.

The air filter removes foreign substances such as dust and dust contained in the air when the combustion air sucked into the gas turbine is taken in the air and purifies the purified air to supply it to the gas turbine. Is weak at high temperature, and there is a problem that the foreign matter is not removed well.

In addition, most of the microfibers usually produced are manufactured by a spinning process such as melt spinning, dry spinning, wet spinning, or the like, in which the polymer solution is forced extruded and spun into fine holes by a mechanical force. However, the diameter of the nonwoven fabric produced in this manner is in the range of about 5 to 500 mu m, and it is difficult to produce nanofiber fibers of 1 mu m or less. Therefore, a filter composed of such a large-diameter fiber can filter contaminant particles having a large diameter, but it is practically impossible to filter nano-sized contaminant particles.

In order to solve the above problems, various methods for fabricating nano-sized fibers (nonwoven fabric) have been developed and used. Among them, a method of forming an organic nano-nonwoven fabric includes a nano- Formation of nano nonwoven fabric by polymerization under silica catalyst, formation of nanofiber nonwoven fabric by carbonization process after melt spinning, and formation of nanofiber nonwoven fabric by electrospinning of polymer solution or melt.

When the nanofiber nonwoven fabric filter is fabricated using the thus produced nanofiber nonwoven fabric, the non-woven fabric filter has a larger specific surface area than the nanofiber nonwoven filter having a larger diameter, has flexibility for surface functional groups, and has nano pore size. Can be efficiently removed.

However, since the production cost of the filter using the nano-nonwoven fabric is very high and it is not easy to control the various conditions for production, the filter using the nano-nonwoven fabric can not be produced at a relatively low unit price.

SUMMARY OF THE INVENTION The present invention has been made to solve the above-mentioned problems, and it is an object of the present invention to produce a web having improved adhesion by forming two or more layers of nanofibers between thermoplastic polyurethane substrates.

To achieve these and other advantages and in accordance with the purpose of the present invention, as embodied and broadly described herein, there is provided a thermoplastic polyurethane foam comprising: a first thermoplastic polyurethane base; A first nanofiber having a basis weight of 0.1 to 2 g / m < 2 > formed by electrospinning a first polymer spinning solution on the first thermoplastic polyurethane base; A second nanofiber having a basis weight of 0.1 to 2 g / m < 2 > formed by electrospinning a second polymer spinning solution on the first nanofiber; And a second thermoplastic polyurethane substrate laminated on the second nanofibers, wherein the nanofibrous web has improved adhesion.

Here, the first polymer spinning solution and the second polymer spinning solution are different from each other, and each of the polypropylene (PP), polyethylene terephthalate (PET), polyvinylidene fluoride, nylon, polyvinyl acetate, polymethylmethacrylate , Polyacrylonitrile (PAN), polyurethane (PUR), polybutylene terephthalate (PBT), polyvinyl butyral, polyvinyl chloride, polyethyleneimine, polyolefin, polylactic acid (PLA) Made of polyethylene naphthalate (PEN), polyamide (PA), polyvinyl alcohol (PVA), polyethylene imide (PEI), polycaprolactone (PCL), polylactic acid glyceric acid (PLGA), silk, cellulose and chitosan , And the second polymer spinning solution is polyurethane, and the second polymer spinning solution is polyvinylidene fluoride or polyamide It is more preferable to contain.

Preferably, the first nanofiber and the second nanofiber include a nanofiber layer having a large fiber diameter and a nanofiber layer having a small fiber diameter.

It is preferable that the first nanofiber and the second nanofiber have different weights in the transverse or longitudinal direction.

Here, the nanofiber web is preferably for a filter, and more preferably for a liquid filter.

According to another aspect of the present invention, there is provided a method of manufacturing a polymer electrolyte fuel cell, comprising the steps of: supplying a first polymer spinning solution to a nozzle of a front end block of an electrospinning apparatus; and supplying a second polymer spinning solution to a nozzle of a rear end block of the electrospinning apparatus; Forming a first nanofiber layer having a basis weight of 0.1 to 2 g / m < 2 > on the first thermoplastic polyurethane substrate by electrospinning the first polymer spinning solution on the first thermoplastic polyurethane substrate; The second polymeric spinning solution is successively electrospun on the first nanofibers to form second nanofibers having a basis weight of 0.1 to 2 g / m < 2 > in the nozzle of the rear end block; And forming a second thermoplastic polyurethane base material on the second nanofibers. The present invention also provides a method of manufacturing an improved nanofiber web having improved adhesion.

In the step of forming the nanofibers, it is preferable to use a bottom-up electrospinning method.

More preferably, the electrospinning device is constituted by two or more electrospinning devices, wherein the bottom-up and top-down electrospinning devices are alternately arranged, or the top-down and bottom-up electrospinning devices are alternately arranged, A flip device for rotating the nonwoven fabric 180 degrees may be provided.

It is preferable that the electrospinning device is electrospinning the polymer spinning solution through the nozzle at a high temperature of 45 to 120 ° C. by using a temperature controller, and the polymer spinning solution is the same as described above.

According to the configuration of the present invention, the objects of the present invention described above can be achieved. Specific effects according to the configuration of the present invention are as follows.

The filter according to the present invention is advantageous in that the thermoplastic polyurethane nonwoven fabric is used as a base material, and can be partially melted in a high temperature laminating environment through its thermoplastic property, so that it can serve as an adhesive without a separate adhesive. In addition, by forming the nanofibers in layers between the substrates, the heat resistance is further improved and the filtering efficiency of the filter is excellent. In addition, an electrospinning device for spinning nanofibers is provided with several blocks, so that mass production of nanofibers is possible.

Also, the nanofibers and filters of the present invention can be used as separators and are preferable. Since the separator made of the nanofibers produced through electrospinning has porosity, the separator prepared from the separator is preferably used as a separator because of its excellent cell performance, and desorption occurs between the substrate and the nanofibers Therefore, it is possible to use a stable separation membrane.

1 is a schematic view of a filter manufactured by the present invention.
2 is a view showing an electrospinning apparatus used in the present invention.
3 is a block diagram of an electrospinning device used in the present invention.
4 is a view showing a nozzle block and a nozzle of an electrospinning apparatus used in the present invention.
5 is a diagram of an electrospinning apparatus having an overflow system and a viscosity control system used in the present invention.
Fig. 6 is a front sectional view showing a tubular body equipped with a coil-shaped heating wire in an electrospinning apparatus having a temperature control device used in the present invention.
7 is a cross-sectional view taken along the line A-A 'in FIG.
FIG. 8 is a front sectional view showing a tubular body equipped with a linear heating wire in an electrospinning apparatus equipped with a temperature control device according to the present invention.
9 is a cross-sectional view taken along the line B-B 'in FIG.
10 is a front sectional view showing a tubular body equipped with a U-shaped pipe in an electrospinning apparatus having a temperature control device used in the present invention.
11 is a cross-sectional view taken along line C-C 'of FIG.
12 is a plan view showing a state in which the nozzle in the spinning solution unit of the present invention is turned on and off in the CD direction.
FIG. 13 is a plan view showing a process of electrospinning the polymer in the CD direction in accordance with the operation of the nozzle in the spinning solution unit shown in FIG. 12; FIG.
14 is a plan view showing a state in which the nozzle in the spinning solution unit of the present invention is turned on and off in the MD direction.
15 is a schematic view schematically showing an electrospinning device including a bottom-up electrospinning device and a top-down electrospinning device according to an embodiment of the present invention.

Hereinafter, preferred embodiments of the present invention will be described in detail with reference to the accompanying drawings. The present invention is not limited to the scope of the present invention, but is merely an example, and various modifications can be made without departing from the technical gist of the present invention.

First, an electrospinning device used in the present invention will be described with reference to the drawings.

Hereinafter, a method of manufacturing a filter according to an embodiment of the present invention will be described, but the present invention is not limited thereto.

Fig. 1 is a schematic view of a filter manufactured by the present invention, Fig. 2 is a view showing an electrospinning device used in the present invention, Fig. 3 is a block diagram of an electrospinning device used in the present invention, Are drawings of a nozzle block and a nozzle of an electrospinning apparatus used in the present invention.

As shown in the drawing, the electrospinning apparatus 10 of the present invention includes a spinning liquid main tank (not shown) in which a spinning liquid is filled and a weighing device for supplying a fixed amount of the polymer spinning solution filled in the spinning liquid main tank (3) in which a plurality of nozzles (2) in the form of a pin are arranged and a polymer spraying liquid in the spinning liquid main tank (1) is discharged from a nozzle A block 20 for accommodating therein a collector 4 spaced apart from the nozzle 2 in order to accumulate the usage liquid and a voltage generating device 1 for generating a voltage to the collector, And a case 8 made of a negative conductor.

In the present invention, one spinning liquid main tank (not shown) is provided. However, in the case where the spinning liquid is composed of two or more spinning liquids, two or more main spinning liquid main tanks may be provided, or one spinning liquid main tanks It is also possible to divide into two or more spaces and supply two or more polymer spinning solution filled in each divided space.

Herein, in the present invention, the electrospinning device 10 uses a bottom-up electrospinning device for spraying the spinning liquid in the upward direction.

Meanwhile, in one embodiment of the present invention, a bottom-up electrospinning device for spraying the spinning solution upward by the electrospinning device may be used, but a top-down electrospinning device for spraying the spinning solution in the downward direction may be used. A composite electrospinning device in which a spinning device is used together may also be used.

With the above structure, the electrospinning apparatus 10 is configured such that the spinning liquid filled in the spinning liquid main tank in the block 20 continuously flows into the plurality of nozzles 2 to which a high voltage is applied through the metering pump And the spinning solution of the polymer supplied to the nozzle 2 is radiated and focused on the collector 13 having a high voltage through the nozzle 2 to form nanofibers (not shown) The fibers are laminated to produce a filter.

In the front end of the electrospinning device 10, there is provided a feed roller 11 for feeding a long sheet on which nanofibers are laminated by spraying a polymer spinning solution in each block 20, Up roller 12 for winding the sheet.

The elongated sheet is provided for preventing and transporting the nanofibers. One end and the other end of the elongated sheet are wound around a feeding roller 11 provided at the front end of the electrospinning device 10 and a winding roller 12 provided at the rear end.

On the other hand, the electrospinning device 10 of each block 20 is installed in the advancing direction (a) of the long sheet with respect to the collector 4. An auxiliary belt 6 is provided between the collector 4 and the long sheet and a long sheet in which nanofibers are stacked and formed on the respective collectors 4 through the auxiliary belts 6 is formed in a horizontal direction Lt; / RTI > That is, the auxiliary belt 6 rotates in synchronization with the conveyance speed of the long sheet, and has the auxiliary belt roller 7 for driving the auxiliary belt 6. The auxiliary belt roller 7 is an automatic roller having at least two frictional forces. Since the auxiliary belt 6 is provided between the collector 4 and the long sheet, the long sheet is smoothly conveyed without being attracted to the collector 4 to which the high voltage is applied.

With the structure as described above, the spinning solution filled in the spinning liquid main tank in the block 20 of the electrospinning device 10 is sprayed onto the elongate sheet placed on the collector 4 through the nozzle 2 , The spinning solution sprayed on the elongate sheet is accumulated, and the nanofibers are laminated. The auxiliary belt 6 is driven by the rotation of the auxiliary belt roller 7 provided on both sides of the collector 4 so that the elongated sheet is conveyed and positioned within the block 20 at the rear end of the electrospinning device 10 And the above-described process is repeatedly performed.

4, the nozzle block 3 includes a plurality of nozzles 2 arranged upward from the discharge port, a tube 43 formed by a row of nozzles 2, a spinning solution storage tank 44, And a spinning liquid circulating pipe (45).

First, the spinning liquid storage tank 44 connected to the spinning liquid main tank to receive and store the spinning solution is connected to the nozzle 2 through the spinning liquid circulating pipe 45 by the metering pump (not shown) And the spinning solution is supplied to the spinning solution. Here, the tube 43 having a plurality of nozzles 2 in a row is supplied with the same spinning solution from the spinning solution storage tank 44, but a plurality of spinning solution main tanks are provided, It is also possible to supply a spinning liquid of different kinds to each of the tubes 43 and radiate them.

When radiated from the discharge port of the plurality of nozzles 2, the overflowed solution is moved to the overflow solution storage tank 41. The overflow solution storage tank 41 is connected to the spinning solution main tank so that the overflow solution can be reused for spinning.

As shown in FIG. 2, the main controller 30 of the present invention controls the amount of spinning solution supplied to the nozzle block 3, 20 controls the voltage of the voltage generating device 1 and controls the feeding speed of each block 20 according to the thickness of the nanofiber and the long sheet base material measured by the thickness measuring device 9. [

The thickness measuring device 9 is provided so as to be opposed to each other with a long sheet stacked with nanofibers positioned at the front end and the rear end of the block 20. The thickness measuring device 9 is connected to the main controller 30 for adjusting the radiation conditions of the electrospinning device 10 so that the thickness measuring device 9 measures the thickness of the nanofiber and the long sheet On the basis of this, the main controller 30 controls the conveying speed of each block 20. For example, in the case of electrospinning, when the thickness of the nanofibers discharged to the block 20 located at the front end portion is measured thinly, the conveying speed of the block 20 located at the rear end portion is reduced, Adjust the thickness uniformly. Also, the main controller 30 increases the discharge amount of the nozzle block 3 and adjusts the voltage intensity of the voltage generator 1 to increase the discharge amount of the nanofibers per unit area, thereby uniformly controlling the thickness of the nanofibers It is possible to do.

The thickness measuring device 9 includes a thickness measuring unit configured to measure a distance between the nanofibers in which the nanofibers are laminated and a long sheet and a pair of ultrasonic longitudinal waves and transverse waves by an ultrasonic measuring method. And the thickness of the nanofiber and the long sheet is calculated on the basis of the distance measured by the pair of ultrasonic measuring apparatuses. More particularly, the present invention relates to a method and a device for measuring the propagation time of longitudinal waves and transverse waves of longitudinal waves and transverse waves, respectively, by projecting ultrasound waves and transverse waves to longitudinal sheets laminated with nanofibers, Measuring the time, measuring a propagation time of the longitudinal wave and the transverse wave and a temperature coefficient of propagation velocity and propagation velocity of the longitudinal wave and the transverse wave at a reference temperature of the long sheet in which the nanofibers are stacked, Is a thickness measuring apparatus for calculating a thickness

The electrospinning device 10 used in the present invention does not change the feed rate from the initial value when the thickness deviation amount of the nanofibers is less than the predetermined value and changes the feed rate from the initial value It is possible to simplify the control of the conveyance speed by the conveyance speed control apparatus. Further, in addition to the control of the conveying speed, the discharge amount and the voltage intensity of the nozzle block 3 can be adjusted. When the thickness deviation amount is less than the predetermined value, the discharge amount of the nozzle block 3 and the voltage intensity are not changed from the initial value , It is possible to control the amount of discharge of the nozzle block 3 and the intensity of the voltage to be changed from the initial value when the amount of deviation of the nozzle block 3 is equal to or larger than the predetermined value. .

The block 20 of the electrospinning apparatus 10 is divided into a front end block 20 located at the front end portion and a rear end block 20 located at the rear end portion according to the radiation position. In the embodiment of the present invention, the number of blocks is limited to two, but it is also possible to have two or more blocks.

In addition, in the present invention, the polymer solution for the same kind is radiated in each block 20, but it is also possible that two or more different polymer solutions are radiated in any one block. In each block 20, It is also possible to emit the polymer spinning solution separately.

In the present invention, the same polymeric spinning solution is radiated in each of the blocks 20a and 20b, but it is also possible to spin different kinds of polymer spinning solutions for each block, and two or more different It is also possible that the polymer spinning solution is radiated. When at least two different kinds of spinning solutions are supplied and radiated for each block 20, it is possible that the polymer nanofibers of different kinds are successively laminated.

In addition, it is also possible to manufacture hybrid nanofibers by constituting two or more polymer types of the spinning solution to be used.

It is also possible to continuously laminate nanofibers having different fiber thicknesses by varying the intensity of the voltage applied to each block 20. In a block 20, the number of nozzles 2 located in the nozzle block 3 It is also possible to form a hybrid nanofiber in which two or more polymers are electrospun and laminated.

In the electrospinning apparatus 10, when the same polymer of the same type is electrospun in each block 20, the nanofibers discharged from the block 20 located at the front end and the nanofibers discharged from the block 20 located at the rear end It is possible to radiate the discharged nanofibers with different fiber thicknesses. For example, in order to make a difference in fiber thickness, it is possible to form nanofibers having different thicknesses by varying the intensity of voltage applied to each block 20 or adjusting the distance between the nozzle 2 and the collector 4 If the spinning liquid is the same and the supply voltage is the same, it is also possible that the diameter of the fiber becomes thicker as the spinning distance becomes closer and the nanofibers of different fiber diameters are formed according to the principle that the fiber diameter becomes narrower as the spinning distance becomes longer . The difference in fiber thickness can be determined by adjusting the concentration of the spinning liquid or by adjusting the feeding speed of the long sheet.

On the other hand, a laminating device 19 is provided at the rear end of the electrospinning device 10 of the present invention. The thermoplastic polyurethane base 5 on which the nanofibers are deposited is finished with the production of the nanofibers through the heating device 19. The heating temperature may be set differently depending on the kind of the thermoplastic polyurethane base material, In the present invention, the polyimide is heated to 150 to 350 DEG C for imidization. Thus, the laminating device 19 applies heat and pressure, and the filter base material on which the nanofibers are laminated, that is, the nanofiber filter is wound on the winding roller 12 to form a nanofiber filter.

The electrospinning device 10 can increase the collecting area to uniform the density of the nanofibers and effectively prevent the droplet phenomenon, thereby improving the quality of the nanofibers, The nanofibers and nanofibers thereof can be mass-produced. In addition, since the material and the electrospinning condition can be controlled in the electrospinning in the block 20 having the nozzle 2 having a plurality of pins, the width and thickness of the nonwoven fabric and the filament can be freely changed and adjusted.

In addition, when the polymer is spun as described above, it is most preferable to spin the polymer under environmental conditions of 30 to 40 DEG C and 40 to 70% of the temperature depending on the polymer material.

In the present invention, the diameter of the nanofiber is preferably 30 to 1000 nm, more preferably 50 to 500 nm.

On the other hand, as shown in FIG. 4, the electrospinning device of the present invention may include a temperature control device 60 for controlling viscosity to maintain fiber viscosity suitable for electrospinning.

As the temperature control device 60, it is possible to use a heating device capable of keeping the viscosity of the high-viscosity polymer solution reused through the overflow low and a cooling device capable of keeping the viscosity of the polymer solution having a relatively low viscosity high, .

In the temperature in the electrospinning region, the temperature of the region where the electrospinning occurs (hereinafter, referred to as the 'radiating region') changes the surface tension of the spinning solution by changing the viscosity of the spinning solution, . ≪ / RTI >

That is, when the temperature of the radiation region is relatively high, the nanofiber having a relatively small fiber diameter is produced when the viscosity of the solution is low, and the nanofiber having relatively large fiber diameter is produced when the viscosity of the solution is relatively high because the temperature is relatively low.

The concentration measuring device for measuring the concentration has a contact type and a non-contact type in direct contact with a solution, and a capillary type concentration measuring device and a disk (DISC) type concentration measuring device can be used as a contact type. A concentration measuring device using the infrared or a concentration measuring device using infrared can be used.

The heating device of the present invention may be an electric heater, a hot water circulating device, a hot air circulating device, or the like. In addition, devices capable of raising the temperature in the same range as the above devices may be borrowed.

As an example of the heating device, the electro-thermal heater may be used in the form of a hot wire, and coil-shaped hot wires 62a and 62b may be mounted inside the tube 43 of the nozzle block 110, (See Figs. 5 to 11).

It is also possible to have the configuration of the linear heat lines 62a and 62b and the U-shaped pipe 63.

As shown in FIG. 5, the heating device includes a nozzle block 110 through which a polymer solution is radiated, a tank (main storage tank, intermediate tank or regeneration tank) and an overflow system 200 (E.g., a transfer pipe that is transferred to the regeneration tank).

The cooling device of the present invention may be a cooling device including a chilling device, and the means for maintaining a constant viscosity of the polymer solution is usually applicable. The cooling device may be provided in at least one of the nozzle block 110, the tank, and the overflow system 200 in the same manner as the heating device, and is used to maintain a certain viscosity of the polymer solution.

In addition, the temperature control device 60 of the present invention includes a sensor for measuring the concentration and a temperature control unit (not shown) for controlling the temperature accordingly.

The sensor is installed in the main storage tank 210, the intermediate tank 220, the regeneration tank 230, the nozzle block 110 or the overflow system 200 to measure the concentration of the flushing liquid in real time, The heating device and / or the cooling device is operated so that the viscosity is kept constant in the device 60. [

The concentration of the polymer solution re-supplied through the overflow system 200 of the present invention is 20 to 40%, which is a high concentration solution compared to the concentration of the polymer solution used in conventional electrospinning of 10 to 18%.

In addition, the temperature of the polymer solution according to the concentration of the polymer solution is adjusted to 45 to 120 캜, rather than the room temperature, in order to maintain the viscosity of the polymer solution to be supplied again.

Meanwhile, the viscosity of the polymer solution of the present invention is preferably 1,000 to 5,000 cps, more preferably 1,000 to 3,000 cps. If the viscosity is 1,000 cps or less, the quality of the nanofibers to be electrospun is poor, and if the viscosity is 3,000 cps or more, the polymer solution can not be easily discharged from the nozzle 42 during the electrospinning, resulting in a slow production rate.

In addition, the present invention is characterized in that as the electrospinning progresses, the viscosity of the polymer solution is constant and the ease of spinning during electrospinning is excellent, and the concentration of the polymer solution is increased. As a result, the amount of solids in the nanofiber, There is an increasing effect.

In addition, the amount of the residual solvent of the nanofibers using electrospinning is lower than that of the conventional electrospinning, and thus it is possible to produce nanofibers of excellent quality.

The temperature control device 60 of the present invention measures the viscosity of the polymer solution through the temperature control of the nozzle block 110 or the main storage tank 210 by measuring the concentration of the intermediate tank 220 in an off- Which can be controlled manually, and which can automatically control the temperature of the solution according to the concentration measurement through an automatic control system on-line.

Hereinafter, the thermoplastic polyurethane base used in the present invention will be described.

First, the polyurethane is a polymer of a urethane bond formed by the reaction of a polyisocyanate and a polyalcohol. Polyurethane is excellent in elasticity, abrasion resistance, and processability, and is widely used in industrial, consumer products, and parts. Since the properties of polyurethane vary depending on the type of polyurethane, selection of a product suitable for the application is important.

The polyurethane is classified into two types, thermoplastic polyurethane and thermosetting polyurethane. The thermoplastic polyurethane has excellent characteristics such as strength, formability, chemical resistance, oil resistance and wear resistance. BACKGROUND ART [0002] Flexible nonwoven fabrics made of thermoplastic polyurethane (hereinafter referred to as "TPU") have been used for applications including clothing, sanitary materials, and sporting goods materials due to their high elasticity, low residual strain and excellent air permeability. The thermoplastic polyurethane nonwoven fabric produced by the so-called melt-blow spinning method has excellent stretchability, flexibility and air permeability, and has been conventionally used as a side band of paper diapers, a base fabric of first-aid bandages, And the like, which are relatively soft and stretchable, such as sports apparel, stretch cotton pads, and the like.

The process for producing the thermoplastic polyurethane is well known. That is, it is prepared by reacting a linear polyol containing a hydroxy end group such as a polyester polyol or a polyether polyol with a diisocyanate compound containing an isocyanate group at both terminals, and optionally, a chain extender, a monoamine compound Terminal stopping agents, and other additives.

Examples of the polyol include various diols comprising a linear homo or copolymer such as a polyester diol, a polyether diol, a polyester amide diol, a polyacryl diol, a polythioester diol, a polythioether diol, a polycarbonate diol, ≪ / RTI > may be used. More specific examples include polyalkylene ether glycols such as polyoxyethylene glycol, polyoxypropylene glycol, polytetramethylene ether glycol, copolymer polyether glycol composed of tetramethylene group and 3-methyl tetra ketylene group.

As the diisocyanate compound serving as a hard segment, an aromatic, aliphatic or alicyclic diisocyanate is used, for example, 4,4'-diphenyl ketadiisocyanate, 1,3- and 1,4-cyclohexylene diisocyanate, 1,6-hexamethylene diisocyanate, trimethylene diisocyanate, tetramethylene diisocyanate, isophorone diisocyanate, and the like, but are not limited thereto.

Examples of the chain extender include a diamine compound or a diol compound. Examples of the chain extender include a diamine compound such as methylene diamine, ethanol diamine, 1,2-propylene diamine and the like, and a diamine compound such as ethylene glycol, 1,3-propanediol, , Neopentyl glycol, and the like, but are not limited thereto.

Examples of the terminal terminating agent include monoamine compounds such as monoethanolamine, diethanolamine and diisopropylamine.

On the other hand, the number average molecular weight of the thermoplastic polyurethane is preferably 1,000 to 100,000.

In the present invention, such a thermoplastic polyurethane is used as a base material. The nonwoven fabric is produced by preparing a web (a state in which fibers are repeatedly laminated) and entangling the fibers physically and chemically together.

Typical nonwoven fabrication processes involve web formation and web bonding processes. The general process is used only for single-fiber nonwovens, and this process is not necessary because longwoven nonwovens use filaments by spinning. In the case of non-woven fabric, it is put in a compressed bale state, so that the nonwoven fabric must undergo the process of compressed fibers. The formation process of the web is a necessary process for forming the nonwoven fabric. The dry nonwoven fabric forms the web in the air, whereas the wet nonwoven fabric disperses the fibers to obtain the web. Therefore, in the dry nonwoven fabric, the arrangement of the fibers is mostly directional, but the wet nonwoven fabric has a random irregular arrangement of the fibers. However, the development of a random card machine for dry nonwovens also makes it possible to obtain a web having no directionality depending on its application.

As a method of forming the web, a spun bond method using long fibers produced by dissolving radiation from raw pellets, a dry method of forming a web by arranging short fibers in a predetermined direction in a card machine or the like, And a wet method in which the water is homogeneously dispersed and drained to form a web.

Methods for entangling the fibers include a thermal bond method in which a thermally soluble fiber is mixed with a web and a thermal roll is used, a chemical bond method in which a binder is bonded (adhered fat), a barb of a needle A needle punch method in which fibers can be entangled with each other, and a meltblown method capable of randomly forming a web by impacting filaments with high-pressure air at the time of producing the fibers and capable of producing a web having a diameter of 0.5 to 30 microns .

Among them, the thermoplastic polyurethane base used in the present invention is preferably produced by the meltblown method, the spunbond method and the needle punch method among the above methods. The principle of the meltblown method is a melt spinning method using a thermoplastic resin, in which a high-temperature and high-pressure airflow is introduced into the outlet of the spinning nozzle to stretch and open the fibers, and then the fibers are accumulated on a collecting conveyor. The nonwoven fabric by this method has an advantage of being excellent in flexibility, impermeability and insulation. Generally, a thermoplastic polyurethane nonwoven fabric is produced by a meltblown spinning method. A general method of meltblown spinning will be described below. That is, the molten thermoplastic polymer is fed to nozzle holes arranged in a row, the molten polymer is continuously extruded from the nozzle holes, the hot gas is jetted at high speed from the slits arranged on both sides of the nozzle hole group, The polymer extruded from the nozzle holes is thinned and cooled to form continuous filaments and then the continuous filament group is accumulated on a moving conveyor net or the like to adhere the filaments to each other by the self-adhesiveness of the filaments themselves.

On the other hand, the spunbond method is a method in which a raw material is spun and self-bonded by heat to form a nonwoven fabric. It is a technology for forming a web by spun polypropylene or polyethylene terephthalate mainly by self-adherence by heat, and there is an advantage that the fabric design is easy.

In addition, in the case of the needle punching method, fibers are physically manufactured by combining webs using special needles, and it is possible to diversify the thickness of the product by the number of punching of needles and the density of needles.

The thermoplastic polyurethane nonwoven fabric produced by such a nonwoven fabric manufacturing method is preferably used as the base material used in the present invention. The thermoplastic polyurethane nonwoven fabric substrate has a structure in which the pores are small and uniformly dispersed and distributed in spite of the fact that the surface area is very low, very thin, soft and soft, and has air permeability as well as excellent elongation and expansion characteristics. It is also possible to attach a thinner, soft and soft composite material when combined with other members in that it can be composed of a thin nonwoven fabric. The thermoplastic polyurethane has a melting point of 80 to 200 ° C. Therefore, there is an advantage that the thermal adhesiveness is good and can be used for thermal bonding after the heat treatment. On the other hand, the basis weight of the base material is preferably 10 to 150 g / m < 2 >. If the basis weight is less than 10 g / m < 2 >, the physical properties of the base material are deteriorated. If the basis weight exceeds 150 g / m & .

The thermoplastic polyurethane nonwoven fabric can be hydrophobic or hydrophilic, can be introduced in color, and can be partially melted in a high-temperature laminating environment due to its thermoplastic characteristics, so that the thermoplastic polyurethane non- There is a possible advantage.

Hereinafter, the polymer of the spinning solution used in the present invention will be described.

The first polymer spinning solution and the second polymer spinning solution are not particularly limited, and examples thereof include polypropylene (PP), polyethylene terephthalate (PET), polyvinylidene fluoride, nylon, polyvinyl acetate, (PU), polybutylene terephthalate (PBT), polyvinyl butyral, polyvinyl chloride, polyethyleneimine, polyolefin, polylactic acid (PLA), poly (PVA), polyethylene naphthalate (PEN), polyamide (PA), polyvinyl alcohol (PVA), polyethylene imide (PEI), polycaprolactone (PCL), polylactic acid glyceric acid Cellulose and chitosan. Among them, polypropylene (PP) materials and heat-resistant high molecular materials such as polyamide, polyimide, polyamideimide, poly (meta-phenylene isophthalamide), polysulfone, Aromatic polyesters such as ether ketone, polyetherimide, polyethylene terephthalate, polytrimethylene terephthalate and polyethylene naphthalate, polytetrafluoroethylene, polydiphenoxaphospazene, polybis [2- (2-methoxy Propoxyphenyl) phosphazene], polyurethane copolymers including polyurethane and polyether urethane, cellulose acetate, cellulose acetate butyrate, cellulose acetate propionate and the like are commonly used . More preferably, one or more selected from the group consisting of polyurethane, polyvinylidene fluoride and polyamide is preferably used.

The polymer spinning solution is a solution prepared by dissolving a polymer, which is a synthetic resin material capable of electrospinning, in a suitable solvent, and the type of solvent is not limited as long as it can dissolve the polymer. For example, methyl, ethyl, propyl, isopropyl, n-butyl, isobutyl, isopropyl, n-butyl, isobutyl, sec-butyl, Isobutyl alcohol, isopropyl alcohol, methyl alcohol, ethanol, aliphatic compounds such as hexane, tetrachlorethylene, acetone, and glycol groups such as propylene glycol, diethylene glycol, isobutyl ketone, methyl ethyl ketone, aliphatic hydroxyl group, m- Ethylene glycol, and halogen compounds such as trichlorethylene, dichloromethane, aromatic compounds toluene, xylene, alicyclic compounds such as cyclohexanone, cyclohexane and esters such as n-butyl acetate, ethyl acetate, aliphatic ether Butyl cellosolve, acetic acid 2-ethoxy ethanol, 2-ethoxy ethanol, amide dimethyl formamide, dimethylacetamide, etc. And, it is possible to use a mixture of a plurality kinds of solvents. The polymer spinning solution preferably contains, but is not limited to, an additive such as a conductivity improver.

The polyurethane, which is one of the polymers used in the present invention, can be produced by using a known polyurethane reaction technique. For example, it is possible to prepare an intermediate polymer having an isocyanate group at its terminal by reacting a polyalkylene ether glycol with an excess molar of an organic diisocyanate in an amide polar solvent, then dissolving the intermediate polymer in an amide polar solvent, The polyurethane polymer can be obtained by reacting an end terminator.

In the production of the hydrophilic polyurethane prepolymer, polyether polyols are preferably synthesized in a molar ratio of 0.15 to 0.95 based on 1 to 3 moles of isocyanate.

Examples of the isocyanate include isophorone diisocyanate, 2,4-toluene diisocyanate and its isomers, diphenylmethane diisocyanate, hexamethylene diisocyanate, lysine diisocyanate, trimethylhexamethylene diisocyanate, bis (2-isocyanate ether) , 3,3'-dimethyl-4,4'-diphenylmethane diisocyanate, 1,6-hexane diisocyanate, 4,4'-biphenylene diisocyanate, 3,3'-dimethylphenylene diisocyanate, 1,3-xylene diisocyanate, and the like. Of these, diphenylmethane diisocyanate, 2,4-xylene diisocyanate, 1,4-xylene diisocyanate, - toluene diisocyanate and its isomers, p-phenylenediisocyanate, isophorone diisocyanate, hexamethylene diisocyanate It is better to use it.

The polytetrahypolyol includes an ethylene oxide / propylene oxide random copolymer having three or more hydroxyl groups in the molecule and having a molecular weight of 3,000 to 6,000 and an ethylene oxide content of 50 to 80%, a polyoxyethylene / propylene oxide random copolymer having two or more hydroxyl groups in the molecule, Propylene oxide random copolymer having 3 hydroxyl groups in the molecule and a molecular weight of 3,000 to 6,000 and an ethylene oxide content of 50 to 80% by weight, based on the weight of polypropylene glycol having a molecular weight of 3,000 to 4,000, Should be used alone. However, in order to control the physical properties, a mixture of a polyisocyanate compound and a polyisocyanate compound not mentioned above may be used.

On the other hand, the hydrophobic polyurethane used in the present invention has a structure in which a firing group is branched, which is obtained by reacting a polyalkylene oxide with a polyfunctional substance, a diisocyanate and water, and reacting the obtained product with a hydrophobic monofunctional active hydrogen- Lt; RTI ID = 0.0 > isocyanate. ≪ / RTI > The hydrophobic group may be independently selected from the group consisting of alkyl, aryl, arylalkyl, alkenyl, arylalkenyl, cycloaliphatic, perfluoroalkyl, carbocylic, polysycyl and composite resin, The aryl, arylalkyl, arylalkenyl, alicyclic, and polycyclyl hydrophobic groups include from 3 to 40 carbon atoms. The term " alkyl "

On the other hand, polyvinylidene fluoride (PVDF) (hereinafter referred to as PVDF) used in the present invention is one of fluorine-based polymers, and the fluororesin contains fluorine, which is excellent in thermal and chemical properties.

[Reaction Scheme 1]

PVDF is prepared by the same process as in the above reaction formula 1, and has a melting point (177) and a density (1.78) lower than those of other fluororesin, and is cheap in chemical cost and low in unit cost. It is also used as an advanced paint for exterior walls.

In addition, PVDF is a representative organic material exhibiting piezoelectricity, and many studies have been conducted since the 1960s. In PVDF polymer, four kinds of crystals are mixed, and it can be divided into at least four types of α, β, γ and δ type depending on crystal form. Among them, β-type crystals of PVDF are filled with trans-type molecular chains in parallel, and all of the permanent dipoles of the monomers are aligned in one direction and exhibit large spontaneous polarization. This means that PVDF molecules are arranged regularly through stretching to impart piezoelectricity by giving anisotropy to the aggregated state. In order to improve such piezoelectric properties, various methods for increasing the? -Form crystal in the PVDF fiber have been studied.

The polyamide as one of the polymers used in the present invention means a general term of a polymer linked by an amide bond (-CONH-) and can be obtained by condensation polymerization of a diamine and a dicarboxylic acid. Polyamides are characterized by amide bonds in the molecular structure, and their physical properties vary depending on the ratio of amide groups. For example, when the ratio of amide groups in the molecule is increased, specific gravity, melting point, absorbency, rigidity and the like are increased.

In addition, polyamide is a material used in a wide range of fields such as clothing, tire cord, carpet, rope, computer ribbon, parachute, plastic and adhesive due to its excellent resistance to corrosion, abrasion resistance, chemical resistance and insulation.

Generally, polyamides are classified into aromatic polyamides and aliphatic polyamides. Representative aliphatic polyamides include nylon. Nylon is originally a trademark of DuPont, Inc., but is now used as a generic name.

Nylon is a hygroscopic polymer and is sensitive to temperature. Representative nylons include nylon 6, nylon 66, and nylon 46.

First, nylon 6 is characterized by excellent heat resistance, moldability and chemical resistance, and is produced by ring-opening polymerization of ε-caprolactam in order to produce it. Nylon 6 means that caprolactam has 6 carbon atoms.

[Reaction Scheme 2]

On the other hand, nylon 66 is generally similar in properties to nylon 6, but is superior in heat resistance to nylon 6 and superior in self-extinguishing and abrasion resistance. Nylon 66 is prepared by dehydration condensation polymerization of hexamethylenediamine and adipic acid.

[Reaction Scheme 3]

Nylon 46 is also excellent in heat resistance, mechanical properties and impact resistance, and has a high processing temperature. Nylon 46 is prepared by polycondensation of tetramethylenediamine and adipic acid. Diaminobutane (DAB), a raw material, is prepared from the reaction of acrylonitrile with hydrogen cyanide. In the first stage of the polymerization operation, a salt is formed from diaminobutane and adipic acid, and the mixture is polymerized under appropriate pressure The prepolymer is converted into a prepolymer and the solid of the prepolymer is polymerized at a solid state by treatment at about 250 ° C in the presence of nitrogen and water vapor.

Nylon 46, in particular, is characterized by a high amide concentration and a regular arrangement between the methylene and amide groups. The melting point of nylon 46 is about 295 ° C, which is higher than that of other types of nylon, and has attracted attention as a resin having excellent heat resistance due to the above characteristics.

Hereinafter, a method of manufacturing a nanofiber filter having improved adhesion produced by electrospinning a polymer spinning solution on a thermoplastic polyurethane substrate using the electrospinning apparatus 10 will be described.

At this time, in the present invention, the above-mentioned polymer is used as the polymer of the spinning solution, and the thermoplastic polyurethane base 100 is used as the elongated sheet.

Wherein the first polymeric spinning solution and the second polymeric spinning solution are different from each other and each comprise at least one of polypropylene (PP), polyethylene terephthalate (PET), polyvinylidene fluoride, nylon, polyvinylacetate, polymethylmethacrylate, poly (PBA), polyvinyl butyral, polyvinyl chloride, polyethyleneimine, polyolefin, polylactic acid (PLA), polyvinyl acetate (PVAc), polyethyleneterephthalate In the group consisting of naphthalate (PEN), polyamide (PA), polyvinyl alcohol (PVA), polyethylene imide (PEI), polycaprolactone (PCL), polylactic acid glyceric acid (PLGA), silk, cellulose and chitosan It is preferable that the first polymer spinning solution is polyurethane, and the second polymer spinning solution is polyvinylidene fluoride or It may comprise a polyamide.

First, referring to FIG. 1, the first polymer and the second polymer are dissolved in an organic solvent to prepare a first polymer spinning solution and a second polymer spinning solution. The first polymer spinning solution and the second polymer spinning solution are supplied to respective spinning solution main tanks of the electrospinning device 10, and the first polymer spinning solution and the second polymer spinning solution are supplied through a metering pump to a nozzle Is continuously supplied in a constant amount into the plurality of nozzles 2 of the block 3.

The polymer spinning solution supplied to each of the nozzles 2 is injected onto the thermoplastic polyurethane base material 5 while being radiated and focused on the collector 4 having a high voltage through the nozzle 2 to form the polymer nanofibers. In the apparatus in which the first polymer nanofibers are laminated in the front end block 20a of the electrospinning device 10, the feed roller 11 and the feed roller 11, which are operated by driving a motor (not shown) Is transferred from the front end block 20a into the rear end block 20b by the rotation of the auxiliary belt 6 driven by the rotation of the auxiliary belt 6. [

The second polymer spinning solution supplied to the main tank into which the second polymer spinning solution is injected in the rear end block 20b is continuously supplied into the plurality of nozzles 2 of the nozzle block 3 to which a high voltage is applied through the metering pump .

At this time, the front end block 20a is referred to as a first feeding device and the rear end block 20b is referred to as a second feeding device.

More specifically, the first main tank for storing the electrospinning liquid of the present invention stores the first polymer spinning solution and the second main tank stores the second polymer spinning solution, and the first and second supply devices And is designed to have a closed cylindrical shape as a whole, and serves to supply the spinning solution continuously injected from the spinning liquid tank for each section. The nozzle block is divided into two sections, and the first and second feeding devices are provided in the respective sections, and the spinning liquid is supplied to the first feeding device through the first heat-resistant polymer spinning solution and the second feeding device is fed with the second heat- Lt; / RTI >

In the present invention, the voltage of the front end block 20a of the electrospinning device 10 is lowered so that the nanofibers having a large fiber thickness are laminated on the substrate, the voltage of the rear end block 20b is increased, The nanofiber filter is formed by laminating thin nanofibers on the thick nanofibers. However, it is also possible that the nanofibers having a small fiber diameter are emitted from the front end block 20a and the nanofibers having a large fiber thickness are emitted from the rear end block 20b.

The length of the section defined by the nozzle block can be adjusted according to the thickness of each layer constituting the filter media.

Further, the collector of the grounded collector can be controlled to be moved in one direction, and a continuous process of forming a continuous nanofiber layer can be performed. The present invention can simplify the manufacturing process of the double-sided filter material through such a process, .

The thickness of the polymer membrane, the diameter of the fiber, and the mechanical characteristics of the shape of the fiber can be arbitrarily controlled by controlling the electrospinning process conditions such as the intensity of the applied voltage, the kind of the polymer solution, the viscosity of the polymer solution, .

In the laminating apparatus 19, the nanofibers on the substrate thus prepared are covered with a cover made of a material different from that of the conventional substrate to form a nanofiber layer between the substrate and the substrate.

The preferred electrospinning process conditions are that the spinning liquid transferred to the spinning liquid supply tube is discharged to the collector through the multiple tubular nozzles to form fibers, and the nanofibers electrospun from the tubular nozzle are discharged by the air injected from the air supply nozzle It spreads widely and is collected on the collector to widen the collecting area and to make the density of the particles uniform. The excess flushing liquid which is not fibrous in the tubular nozzle is collected in the overflow removing nozzle and then moved to the flushing liquid supply plate through the temporary storage plate of the overflow liquid.

When manufacturing nanofibers, it is preferable that the speed of air in the air supply nozzle is 0.05 m to 50 m / sec, more preferably 1 to 30 m / sec. If the velocity of the air is less than 0.05 m / sec, the collecting area of nanofibers is not so low and the collecting area is not greatly improved. If the velocity of the air exceeds 50 m / sec, The more serious problem is attached to the collector in the form of a thick thread rather than the nanofiber, thereby causing a serious problem that the formation of the nanofiber is significantly deteriorated.

In addition, the spinning solution which is excessively supplied to the top of the nozzle block is forcibly transferred to the spinning liquid main tank by the spinning solution discharging device.

In order to promote the formation of fibers by the electric force, a voltage of 1 kV or more, more preferably 20 kV or more, generated in the voltage generator is applied to the conductive plate and the collector provided at the lower end of the nozzle block. It is more advantageous in terms of productivity to use an endless belt as the collector. The collector preferably reciprocates a predetermined distance in the left and right directions to uniform the density of the nanofibers.

When the nanofibers formed on the collector are wound on the winding roller through the web supporting roller, the manufacturing process of the nanofibers is completed.

The nanofiber filter manufactured as described above is preferably applied to a liquid filter, but is not limited thereto.

On the other hand, the nanofibers produced according to the present invention may be laminated by electrospinning in different widths in the width direction, i.e., in the CD direction or in the transverse direction, or different in basis weight in the longitudinal direction, i.e., the MD direction. In this case, the CD direction is the cross direction, which means the direction perpendicular to the MD direction (Machine Direction), the MD direction is referred to as the longitudinal direction / longitudinal direction, and the CD direction is referred to as the width direction / transverse direction. Basis Weight or Grammage is also defined as mass per unit area, i.e., grams per square meter (g / m 2) as a preferred unit.

12 is a plan view showing a state in which the nozzles in the spinning liquid unit of the present invention are turned on and off in the CD direction and Fig. 13 is a plan view showing a state in which the basis weight of the polymer in the CD direction, As described above, the operation of the nozzles in the spinning solution unit can be electrically turned on and off to form nanofibers having different basis weights in the CD direction. Fig. 14 is a plan view showing a state in which the nozzle in the spinning solution unit of the present invention is turned on and off in the MD direction. As described above, the operation of the nozzle in the spinning solution unit is electrically turned on and off, Nanofibers can be formed.

Further, the filter according to the present invention can be manufactured by using the electrospinning device 1 configured by including the bottom-up electrospinning device 10 and the top-down electrospinning device 30 as shown in Fig.

At this time, it is preferable that the bottom-up electrospinning device and the top-down electrospinning device are arranged at a predetermined interval, and the bottom-up electrospinning device is positioned at the front end and the top-down electrospinning device is positioned at the rear end, .

It is also preferable that the electrospinning device is constituted by three or more electrospinning devices, the bottom-up electrospinning device and the top-down electrospinning device are alternately arranged, and the flip device 20 is provided between the electrospinning devices Do.

When the three or more electrospinning apparatuses are arranged alternately, the bottom-up electrospinning apparatus can be placed alternately with the bottom-up electrospinning apparatus placed in the front end first, but it is also possible to arrange the bottom-down electrospinning apparatus first and then alternately.

A flip device is provided between the bottom-up electrospinning device and the bottom-up electrospinning device according to the present invention. The flip device is positioned between the electrospinning devices, And the lower surface serves to rotate the upper surface.

In the electrospinning device according to the present invention, the polymer spinning solution filled in the spinning liquid main tank of the bottom-up electrospinning device is injected onto the support on the collector through the nozzle, After the sprayed first polymer spinning solution is accumulated, the first nanofibers are formed, and the lower surface of the support on which the first nanofibers are stacked by the flip device is rotated 180 degrees to the upper surface of the support having the nanofibers laminated thereon.

Thereafter, a second polymer spinning solution, which is transported onto the collector of the top-down electrospinning device and filled in the spinning solution main tank of the top-down electrospinning device, is placed on a support on which the first nanofibers transferred onto the collector of the top- And the second nanofibers are stacked on the first nanofibers by being electrospun through the nozzles.

Thereafter, a post-process is performed by a laminating apparatus 40 for laminating a nanofiber web and a support (substrate) manufactured through the bottom-up and top-down electrospinning apparatuses.

In the present invention, the flip device is provided between the bottom-up and top-down electrospinning devices so that the arrangement of the electrospinning devices is arranged in parallel to the horizontal direction, or each of the electrospinning devices is arranged in the vertical direction It is possible to arrange each electrospinning device in the U direction by using a bottom-up electrospinning device. By using a bottom-up electrospinning device, productivity is improved by using a downward electrospinning device. By using a flip device, There is an advantage that lamination of a nanofiber web can be achieved.

BEST MODE FOR CARRYING OUT THE INVENTION Hereinafter, the present invention will be described in detail with reference to examples. However, the embodiments according to the present invention can be modified into various other forms, and the scope of the present invention should not be construed as being limited to the embodiments described below. The embodiments of the present invention are provided to enable those skilled in the art to more fully understand the present invention.

Example  One

13% by weight of polyurethane (Pellethane 2363-80AE from DOW, USA) was dissolved in 87% by weight of N-dimethylacetamide (DMAc) solvent to prepare a polymer spinning solution having a concentration of 13% Connected spinning liquid was put into the main tank.

A spinning solution having a concentration of 15% by weight prepared by dissolving polyvinylidene fluoride having a weight average molecular weight (Mw) of 50,000 in dimethylacetamide (N, N-dimethylacetamide, DMAc) was added to a spinning solution And put into the main tank.

Afterwards, the spinning liquid was supplied to the nozzles in each block in the main tank, and the electrospinning was performed. At this time, polyurethane nanofibers were laminated on the thermoplastic polyurethane base material having a basis weight of 30 gsm by electrospinning conducted in the front end block to have a basis weight of 0.5 gsm, and the polyurethane nano- A polyvinylidene fluoride nanofiber is laminated on the fiber so that the basis weight is 0.5 gsm, and then a thermoplastic polyurethane base material having a basis weight of 30 gsm is placed on the polyurethane nanofiber and laminated to form a nanofiber To form a filter. At this time, electrospinning was carried out under the condition of a distance between the electrode and the collector of 40 cm, an applied voltage of 20 kV, a spinning solution flow rate of 0.1 mL / h, a temperature of 22 캜 and a humidity of 20%.

Example  2

13% by weight of polyurethane (Pellethane 2363-80AE from DOW, USA) was dissolved in 87% by weight of N-dimethylacetamide (DMAc) solvent to prepare a polymer spinning solution having a concentration of 13% Connected spinning liquid was put into the main tank. In addition, a spinning solution having a concentration of 15% by weight, which was prepared by dissolving nylon 6 in formic acid, was introduced into the spinning liquid main tank connected to the rear end block.

Afterwards, the spinning liquid was supplied to the nozzles in each block in the main tank, and the electrospinning was performed. At this time, polyurethane nanofibers were laminated on the thermoplastic polyurethane base material having a basis weight of 30 gsm by electrospinning conducted in the front end block to have a basis weight of 0.5 gsm, and the polyurethane nano- The polyamide nanofibers were laminated so that the basis weight was 0.5 gsm on the fiber, and then a thermoplastic polyurethane base material having a basis weight of 30 gsm was placed on the polyurethane nanofibers to form a filter having the nanofibers formed on the base material and the substrate surface Respectively. In the electrospinning process, electrospinning was carried out under the conditions of a distance of 40 cm between the electrode and the collector, an applied voltage of 20 kV, a spinning solution flow rate of 0.1 mL / h, a temperature of 22 ° C. and a humidity of 20%.

Comparative Example  One

A meta-aramid dope is prepared by dissolving a meta-aramid having a viscosity of 50,000 cps and a solid content of 20% by weight in dimethylacetamide (DMAc). A 6 m-thick meta-aramid nanofiber was laminated on a cellulose substrate having a basis weight of 30 gsm under the conditions of a distance of 40 cm between the electrode and the collector, an applied voltage of 15 kV, a spinning liquid flow rate of 0.1 ml / h, a temperature of 22 캜 and a humidity of 20% Thereby forming a filter medium.

- Evaluation of adhesion between substrate and nanofiber

After the filters prepared in Examples 1 and 2 and Comparative Example 1 were washed five times, it was confirmed whether or not the substrate and the nanofibers were desorbed.

- Evaluation of heat shrinkage

A 5 cm x 2.5 cm nanofiber filter was placed between two slide glasses, clamped with a clip, allowed to stand at 150 < 0 > C for 30 minutes and then measured for shrinkage.

- Filtration efficiency measurement

The DOP test method was used to measure the efficiency of the fabricated nanofiber filter. The DOP test method is to measure the dioctyl phthalate (DOP) efficiency with an automated filter analyzer (AFT) of TSI 3160 from TSI Incorporated, which can measure the filter efficiency of the filter media material.

The automation analyzer is a device that automatically measures the velocity of air, DOP filtration efficiency, air permeability (permeability), etc. by passing DOP through the filter sheet by making particles of desired size and is a very important device for high efficiency filter.

The DOP% efficiency is defined as:

DOP% efficiency = 1 - 100 (DOP concentration downstream / DOP concentration upstream)

Here, the filtration efficiencies of Examples and Comparative Examples were measured using DOP having a particle size of 0.35 mu m.

Example 1 Example 2 Comparative Example 1 Adhesion evaluation X X O Heat shrinkage (%) 2 2 5 0.35 mu m DOP filtration efficiency (%) 85 89 84

As can be seen from Table 1, it can be seen that the adhesion, heat shrinkage and filtration efficiency are improved as compared with the case of the embodiment using the thermoplastic polyurethane base.

Thus, those skilled in the art will appreciate that the present invention may be embodied in other specific forms without departing from the spirit or essential characteristics thereof. It is therefore to be understood that the embodiments described above are to be considered in all respects only as illustrative and not restrictive. The scope of the present invention is defined by the appended claims rather than the detailed description and all changes or modifications derived from the meaning and scope of the claims and their equivalents are to be construed as being included within the scope of the present invention do.

1: voltage generating device, 2: nozzle,
3: nozzle block, 4: collector,
5: base material, 6: auxiliary belt,
7: roller for auxiliary belt,
8: case, 9: thickness measuring device,
10: electrospinning device, 11: feed roller,
12: take-up roller, 19: laminating apparatus,
20: block, 30: main controller,
41: Overflow solution storage tank, 43: Tubular body,
44: spinning liquid storage tank, 45: spinning liquid circulation pipe,
300: nanofiber.

Claims (13)

A first thermoplastic polyurethane base;
The first thermoplastic polyurethane is formed by first laminating a polymeric electrospinning the spinning liquid on the base material, the basis weight is 0.1 ~ 2g / m ² of the first nano-fibers;
The first and second electrospinning a polymer spinning solution onto the nanofibers are laminated, a basis weight of 0.1 ~ 2g / m ² in a second nano-fibers; And
And a second thermoplastic polyurethane substrate laminated on the second nanofibers,
Wherein the first nanofiber and the second nanofibers have different weights in the transverse or longitudinal direction, respectively.
The method according to claim 1,
The first polymer solution for spinning solution and the second solution for spinning polymer solution are different from each other and are respectively made of polyethylene terephthalate (PET), polyvinylidene fluoride, polyvinyl acetate, polymethylmethacrylate, polyacrylonitrile (PAN), poly (PA), polyamide (PA), polyvinyl alcohol (PA), polyvinyl pyrrolidone (PU), polybutylene terephthalate (PBT), polyvinyl butyral, polyvinyl chloride, polyethyleneimine, polyolefin, Wherein the adhesive layer comprises one selected from the group consisting of polyvinylidene fluoride (PVA), polyethyleneimide (PEI), polycaprolactone (PCL), polylactic acid glycolate (PLGA), silk, cellulose and chitosan This improved nanofiber web.
The method according to claim 1,
Wherein the first polymer spinning solution is polyurethane, and the second polymer spinning solution comprises polyvinylidene fluoride or polyamide.
The method according to claim 1,
Wherein the first nanofiber and the second nanofibers each include a nanofiber layer having a large fiber thickness and a nanofiber layer having a small fiber diameter.
delete The method according to claim 1,
Wherein the nanofiber web is for a filter.
delete delete delete delete delete delete delete

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