Technical Field
[0001] The present invention relates to an apparatus and a method for producing a nanofiber,
which are capable of providing a high-quality nanofiber in a simple structure.
Background of the Invention
[0002] In recent years, demand of a nanofiber is rapidly increasing in accordance with expansion
of use of a fiber having a nanometer-order diameter, namely a nanofiber. In accordance
with expansion of use of the nanofiber, a special nanofiber has been required which
is high in quality and corresponds to purpose. Regarding a nanofiber producing method,
there are conventional methods such as an electrospinning method, a melt blown method
or the like, and there are advantages and disadvantages with each method.
[0003] Patent Document 1 as the above-mentioned background of the invention discloses a
method for producing a nonwoven fabric consisting of a plurality of kinds of fiber
which is made by mixing a solution discharging fiber to a melt blown fiber. Specifically,
by using a solution spinning unit which ejects a spinning solution discharged from
a liquid discharge portion with a gas ejected from a gas discharge portion, the solution
discharge fiber made by discharging and fiberizing the spinning solution is mixed
into a fiber flow of a melt blown fiber delivered from a nozzle by the melt blown
method.
[0004] Furthermore, Non-Patent Document 1 discloses a nanofiber producing method using an
electrospinning method. A conventional electrospinning method for producing the nanofiber
requires solvent for swelling resin, however, Non-Patent Document 1 discloses a configuration
for preventing flashing and explosion caused by using a solvent by swelling by a heat
without using the solvent. Additionally, disadvantages of the nanofiber producing
method using the meld blown method are described in detail.
[0005] Patent Documents 2 to 5 disclose several fiber producing apparatuses. Among Patent
Documents 2 to 5, Patent Document 3 discloses an apparatus as specified in the preamble
of claim 1, which is capable of producing microfibers in the range of 1 to 20 microns
or down to 0.1 micron.
Description of Prior Art
Patent Literature
Non-Patent Literature
Summary of Invention
Problems to be solved by the Invention
[0008] As described in the above-mentioned Non-Patent Document 1, when a fiber diameter
is reduced in the nanofiber producing method of the conventional melt blown method,
it is considered to apply a method for ejecting high-temperature air at high speed
and a method for suppressing discharge of polymer. When the high-temperature air is
ejected at high speed, the fiber diameter is reduced but length of the fiber is shortened
and shredded. On the other hand, when discharge of polymer is suppressed, an amount
of production per unit time is extremely reduced. Accordingly, it is difficult for
either method to achieve mass production of the nanofiber having a good quality. In
an electrospinning method, productivity has been improved, however, an apparatus has
become complicated, countermeasures is required for preventing flashing and explosion,
and cost of manufacture has become expensive.
[0009] The present invention was made in consideration of the above problems, and an object
of the present invention is to provide an apparatus and a method for producing a nanofiber
which is capable of supplying a large amount of the nanofiber having good quality
in nanofiber producing method of a melt blown method, and improving safety by eliminating
factor of flashing and explosion.
Means for Solving the Problems
[0010] According to the present invention, there is provided an apparatus for producing
a nanofiber comprising the features set forth in claim 1.
[0011] According to the present invention, there is provided a method for producing a nanofiber
as specified in claim 8.
[0012] According to the present invention, there is also provided a method for producing
a nanofiber as specified in claim 9.
Effect of the Invention
[0013] According to the present invention, a nanofiber having a smaller diameter and good
quality can be safely produced. Furthermore, when the nanofiber is produced, it is
not necessary to apply an apparatus using high voltage, and a problem of an amount
of production per unit time which is disadvantage for the melt blown method can be
solved by providing a plurality of resin discharge unit.
BRIEF DESCRIPTION OF DRAWINGS
[0014]
Fig. 1 is a partial sectional side view showing an entire structure of an embodiment
1 of a nanofiber producing apparatus according to the present invention.
Fig. 2 is an external plan view showing a head portion and a heating cylinder of the
nanofiber producing apparatus according to the embodiment 1 of the present invention.
Fig. 3 is an external front view showing an end of the head portion of the nanofiber
producing apparatus according to embodiments of the present invention.
Fig. 4 is a cross-sectional view of the nanofiber producing apparatus in Fig. 3, taken
along the line A-A.
Fig. 5 is cross-sectional views of the nanofiber producing apparatus in Fig. 4, taken
along the lines B-B, C-C and D-D, respectively.
Fig. 6 is an explanatory diagram showing resin flow and gas flow in the head portion
of the nanofiber producing apparatus according to the embodiment 1 of the present
invention.
Fig. 7 are explanatory diagrams showing (a) an example of a supporting structure of
a resin discharge unit and (b) another example of a supporting structure of the resin
discharge unit of the nanofiber producing apparatus according to the embodiment 1
of the present invention.
Fig. 8 is a side view showing the entire structure of an embodiment 2 of a nanofiber
producing apparatus according to the present invention.
Fig. 9 is a plan view showing the entire structure of the embodiment 2 of the nanofiber
producing apparatus according to the present invention.
Fig. 10 is a front view showing a structure of the head portion of the embodiment
2 of the nanofiber producing apparatus according to the present invention.
Fig. 11 is an explanatory diagram illustrating a basic concept of the apparatus and
a method for producing the nanofiber according to the present invention.
Detailed Description of Preferred embodiments
[0015] Hereinafter, the preferred embodiment of the present invention will be described
in detail. The present invention is, needless to say, easily applicable to a structure
other than the description of embodiments of the present invention within a scope
not inconsistent with an object of the invention.
[0016] According to the present invention, a nanofiber is formed by supplying a liquid raw
material to fluid (preferably, gaseous fluid) ejected in high pressure. In the description,
a term "GAS" without specifying composition means gases consisting of any composition
and molecular structure. Additionally, in the description, a term "raw material" means
all of materials applicable for forming the nanofiber. In the embodiments hereinafter,
an explanation will be made for an example using synthetic resin as the "raw material",
but not limited thereto, various kinds of composition material will be usable. The
term "liquid raw material" in the description does not limit property of the material
to liquid, and includes "molten raw material" applicable for the embodiment 1 forming
the nanofiber by melting and extruding a solid raw material from an extruding unit.
Moreover, the term "liquid raw material" in the description also includes "dissolved
raw material" applicable for the embodiment 2 which forms the nanofiber by dissolving
in advance a solid or a liquid raw material in a predetermined solvent so that a predetermined
concentration can be obtained, and by feeding by using an appropriate means and discharging
or extruding from a discharge holes. The "liquid raw material" of the present invention
needs property having viscosity enough to supply (eject, discharge) "raw material"
from supplying holes (ejection holes, discharge holes), and "raw material" having
such liquid property is described as "liquid raw material" in the present invention.
[0017] While detail description will be made hereafter, basic concept of the present invention
is common to an apparatus and method for producing the nanofiber explained as the
embodiments 1 and 2 of the present invention, and, as shown in Fig. 11, it is configured
to provide a high-pressure gas ejection unit 71 at a center thereof, and to make an
installation angle of a plurality of discharge units 73a variable, which are arranged
around a high-pressure gas flow 90 ejected from a high-pressure gas ejection unit
71. In other words, a supply angle θ of the liquid raw material to the high-pressure
gas flow 90 is variable. The basic concept of the present invention is, as shown in
Fig. 11, that the discharge unit 73a for discharging the liquid raw material is provided
at the supply angle θ to a central line 91 of the high-pressure gas flow 90, and the
liquid raw material is discharged/supplied from a plurality of the discharge units
73a toward the central line 91 of the high-pressure gas flow 90. The liquid raw material
discharged/supplied from the plurality of discharge units 73a is preferably provided
to be intersected on the central line 91.
[0018] In Fig. 11, arrangement condition of each component is as mentioned above, and positional
relationship is as follows. On the basis of a position of the gas ejection hole (an
opening nozzle) of the high-pressure gas ejection unit 71, "distance a" represents
a distance from the gas ejection hole to the discharge unit 73a, "distance b" represents
a distance from the gas ejection hole to a point that the raw materials discharged
from the discharge unit 73a are intersected, "distance c" represents an opening diameter
of the gas ejection hole, and "distance d" represents a distance between the gas ejection
holes.
[0019] Herein, the discharge unit 73a for discharging the liquid raw material is provided
at the supply angle θ to the central line 91 of the high-pressure gas flow 90. The
raw material supply tangent angle θ is obtained from the following Equation (1)
The raw material supply tangent angle θ is adjustable within a scope of 0°<θ<90°.
As an example, when the "distance a" is equal to 30mm, the "distance c" is equal to
2mm, the "distance d" is equal to 7mm, and pressure of the ejected high-pressure gas
is equal to about 0.15MPa, θ is preferably equal to 20° plus/minus 10°.
[0020] The raw material supply tangent angle θ should be determined by the "distance a",
the "distance b", and the "distance d" between the gas ejection holes, and moreover,
should be determined by relationship among the opening diameter "distance c" of the
high-pressure gas ejection hole, pressure and temperature of the ejected high-pressure
gas.
[0021] According to the apparatus and method for producing the nanofiber of the embodiment
1 of the present invention, a pellet-shaped raw material (resin) fed into a hopper
is supplied and melted in a heating cylinder heated by a heater, and sent to a front
part of the heating cylinder by a screw rotated by a motor. The heating cylinder is
provided with a head portion, and the high-pressure gas is ejected from the gas ejection
hole provided at a center of the head portion. The liquid molten raw material (molten
resin) sent to an end of the heating cylinder is supplied (discharged) from the supply
unit (the discharge unit) of the liquid molten raw material (molten resin) having
a plurality of superfine tubes provided in a downstream side of the gas ejection unit,
through inside of the head portion. A plurality of superfine tubes of the discharge
units of the liquid molten raw material are provided equally around the gas ejection
hole provided at a center. Thereby, the molten resin discharged from the discharge
units of the liquid molten raw material is elongated and the fiber having the nanometer-order
fiber can be obtained.
[0022] According to the apparatus and method for producing the nanofiber of the embodiment
2 of the present invention, configuration is made to eject the high-pressure gas from
the gas ejection hole provided at a center thereof, and the liquid dissolved raw material
is discharged from a plurality of superfine tubes of the discharge units of the liquid
dissolved raw material provided in a downstream side of the discharge units of the
liquid dissolved raw material.
Embodiment 1
[0023] Hereinafter, entire structure of a nanofiber producing apparatus according to the
embodiment 1 of the present invention will be described in detail referring to Figs.
1 to 3.
[0024] A nanofiber producing apparatus 1 as shown in Fig. 1 according to the embodiment
1 of the present invention comprises a hopper 2, a heating cylinder 3, a heater 4
as a heating unit, a screw 5 as an extruding unit, a motor 6 as a driving unit, and
a cylindrical head portion 7. The hopper 2 feeds a resin (a granular synthetic resin
having a fine particle) to be a material for the nanofiber into the nanofiber producing
apparatus 1. The heating cylinder 3 heats and melts the resin supplied from the hopper
2. The heater heats the heating cylinder from outside. The screw 5 is rotatably stored
in the heating cylinder 3 and functions to move the molten resin to the end of the
heating cylinder 3 by rotating. The motor 6 rotates the screw 5 through a connecting
unit 61 (not shown in detail), and the head portion 7 is provided at the end of the
heating cylinder 3. A nanofiber producing apparatus 1 further comprises a gas ejection
hole 71 (an opening nozzle) for ejecting a gaseous hot air from the center area, and
a resin discharge unit inside thereof for discharging the molten resin described below
from the periphery of the gas ejection hole 71 (an opening nozzle) . The high-pressure
gas is supplied to the head portion 7 through a pipe 81 connected to a gas piping
unit 8 as a gas supplying pipe for ejecting the gas from the center area. The gas
piping unit 8 is provided with a heating unit such as a heater or the like (not shown),
and configuration is made to eject a hot air from the gas ejection unit 71 (the opening
nozzle). The head portion 7 and the heating cylinder 3 are connected via a seal portion
9 of a sheet member having a shape of O-ring and a doughnut-shape, and the molten
resin is not leaked to outside of the apparatus thereby.
[0025] A plurality of heaters 4 provided at an outer circumference of the heating cylinder
3 is capable of controlling temperature separately or collectively by a control unit
(not shown). According to the present embodiment, four heaters 4 are provided as shown
in Fig. 1, but not limited thereto, modification is applicable to the number of installation,
size of each heater, and condition of arrangement in conformity to material and property
of the resin to be used, and conditions of a diameter and length of the heating cylinder
3.
[0026] Fig. 2 is a plan view and Fig. 3 is a front view of a nanofiber producing apparatus
1 according to the present embodiment. Figs. 4 to 6 are explanatory diagrams showing
structure of the head portion 7.
[0027] The head portion 7 of the present embodiment, as shown in Fig. 3, is connected to
the pipe 81 into which the high-pressure gas is fed from the outer circumference of
the heating cylinder 3 through the gas piping unit 8. The high-pressure gas from the
pipe 81 is introduced to inside of the head portion 7 and ejected from the gas ejection
hole (the opening nozzle: Fig. 3) provided at the center area. A plurality of resin
discharge units 73 are provided at equal intervals around the gas ejection hole 71.
According to the present embodiment, the resin discharge unit 73 comprises a resin
discharge needle 73a and a resin discharge needle fitting unit 73b having a structure
for fitting the resin discharge needle 73a to the head portion 7.
[0028] The head portion 7 shown in Fig. 3 comprises a heating cylinder cover unit 77 for
covering the end portion of the heating cylinder 3 and a resin discharge unit holding
ring 78 as a means for holding the resin discharge unit 73. The resin discharge unit
holding ring 78 is fixed to the heating cylinder cover unit 77 without fixing means
such as a bolt (without reference number).
[0029] According to this resin discharge unit holding ring 78, if a plurality of the resin
discharge units 73 are provided around the gas ejection hole 71 (the opening nozzle),
there is achieved greatly increasing productivity of the nanofiber having a uniform
diameter and fiber length by arranging a plurality of resin discharge unit 73 at an
equal interval, an equal distance ("distance a" from the gas ejection hole), or an
equal angle (discharge angle θ).
[0030] Referring to Fig. 11, description will be made of positional relationship of the
gas ejection hole 71 (the opening nozzle) and the resin discharge unit 73 provided
around thereof . The gas flow 90 is ejected from the gas ejection hole 71 provided
at a center area of the head portion 7. There is provided a plurality of the resin
discharge units 73 provided around the gas flow 90, and the resin is ejected from
resin discharge holes of the resin discharge needles 73a with a discharge angle θ
to the gas flow 90. The resin discharge holes of the resin discharge needles 73a are
provided forward (in downstream side along with the gas flow 90 from the ejection
holes 71) with "distance a" from the ejection hole 71. Each resin discharge hole of
a plurality of resin discharge needles 73a is provided for discharging the resin forward
with "distance b" from the ejection holes 71 (in the downstream side along with the
gas flow 90 from the ejection holes 71) so as to intersect resins.
[0031] Regarding an arrangement condition of a plurality of resin discharge units 73, it
is also capable of forming a nanofiber having an ununiformed diameter or fiber length
by changing the number of the resin discharge units 73, an arrangement interval, an
arrangement distance ("distance a" from the gas ejection hole), and an arrangement
angle θ. According to use of the produced nanofiber, the arrangement condition of
the resin discharge unit 73 such as the arrangement interval or the like may be appropriately
selected and changed.
[0032] Fig. 4 is a cross-sectional view of the head portion 7 of Fig. 3, taken along the
line A-A. Fig. 5 (a), (b) and (c) are cross-sectional views of main part of the head
portion 7 of Fig. 4, taken along the lines B-B, C-C and D-D, respectively. Fig. 6
is an explanatory diagram showing a flow passage A of the high-pressure gas and a
flow passage B of the molten resin. As shown in Figs. 4 to 6, six resin flow passages
75 (an arrow B in the drawings) are provided at equal intervals corresponding to the
resin discharge unit 73 in the head portion 7. The resin discharge unit 73 is connected
to the heating cylinder 3 through the resin flow passage 75. The molten resin pressed
by rotation of the screw 5 flows into the resin flow passage 75 shown in the cross-sectional
view, taken along the lines D-D of Fig. 5 (c), and through the resin flow passage
75 shown in the cross-sectional view taken along the lines C-C, the molten resin flows
in the resin discharge needle fitting unit 73b shown in the cross-sectional view,
taken along the lines B-B and is discharged from the resin discharge needle 73a. In
this case, as shown in Fig. 4, the gas flow passage 72 (an arrow A in the drawings)
is provided at a center of the head portion 7 so as not to interfere the resin flow
passage 75 (an arrow B in the drawings). Additionally, as shown in a cross-sectional
view, taken along the lines C-C of Fig. 5(b), the gas flow passage 72 is provided
by changing a direction from outside to inside of the head portion 7 through the any
adjacent resin flow passage 75. The gas piping unit 8 is connected to the gas flow
passage 72 through the pipe 81. The high-pressure and high-temperature gas fed from
the gas piping unit 8 through such provided gas flow passage 72 and ejected from the
gas ejection hole 71 (the opening nozzle). The resin flow passage 75 and the gas flow
passage 72 are provided in the head portion 7 so as not to interfere each other. The
numeral reference 79 in Fig. 5(b) represents a screw portion 79 for fitting the pipe
(the gas flow passage) 81 on the heating cylinder cover unit 77.
[0033] In order to adjust the arrangement condition of the resin discharge unit 73 to the
gas flow passage 72, a holding adjusting unit 74 for the resin discharge unit 73 is
provided. A diameter of the resin discharge hole of the resin discharge needle 73a
in the resin discharge unit 73 is very small and the resin discharge needle 73a is
susceptible to the effects of stress such as vibrations of an apparatus and pressure
of the resin, and therefore, the arrangement condition of the previously mentioned
resin discharge unit 73 may be changed and detachment may be occurred from the head
portion 7. It becomes necessary to avoid stress on the resin discharge needle 73a
if an angle of the resin discharge needle 73a is adjusted and changed, and to make
a structure not to detach the resin discharge needle 73a from the head portion 7.
[0034] Fig. 7(a) is an explanatory diagram showing a support structure of the holding adjusting
unit 74 for fixing the resin discharge unit 73 to the resin discharge unit holding
ring 78, and for making a fitting angle adjustable. The resin discharge unit 73 comprises
the resin discharge needle 73a and the resin discharge needle fitting unit 73b, and
the resin discharge needle fitting unit 73b is fixed on the resin discharge unit holding
ring 78 of the head portion 7 by screwing (not shown), engaging and using a fixing
means such as a pin or the like. The resin discharge needle 73a is provided with the
holding adjusting unit 74. This holding adjusting unit 74 comprises a resin discharge
needle gripping unit 74a for gripping the resin discharge needle 73a from the periphery
and a adjusting unit 74b having an adjusting pestle 74c which is retractable and provided
penetrating from outside to inside of the head portion 7. By operating the adjusting
unit 74b, the adjusting pestle 74c is advanced and retracted, and the resin discharge
needle gripping unit 74a is moved in a diameter direction of the head portion 7. Thereby,
the resin discharge needle 73a can be fixed at a desired position and angle. By using
such resin discharge hole support unit 74, the resin discharge unit 73 is adjusted
so that the discharging molten resin is discharged at a desired discharge angle to
the ejection gas flow from the gas ejection hole 71, and is surely fixable at the
angle.
[0035] This structure is useful as the adjusting unit of the discharge angle of the molten
resin against the ejection has flow, and the resin discharge needle 73a has a shape
of very thin pipe. When the nanofiber producing apparatus 1 is operated, big vibration
of the pipe may be occurred on the top thereof by driving the motor 6 and the screw
5, and the holding adjusting unit 74 can suppress the vibration effectively. In Fig.
2 of the present embodiment, six resin discharge units 73 are provided, and the six
holding adjusting unit 74 are also provided, but not limited thereto, the number of
thereof may be appropriately selected in accordance with condition of the resin for
use, an amount of production, property of products.
[0036] Fig. 7(b) shows another example of an angle adjusting function of the resin discharge
unit 73. In this embodiment, the holding adjusting unit 74 comprises a resin discharge
needle gripping unit 74d for gripping the resin discharge needle 73a from the periphery,
and an adjusting unit (not shown) having an adjusting pestle 74e which is retractable
and provided penetrating from outside to inside of the head portion 7. By operating
the adjusting unit, the adjusting pestle 74e is advanced and retracted, and the resin
discharge needle gripping unit 74d is moved in a diameter direction of the head portion
7. Thereby, the resin discharge needle 73a can be fixed at a desired position and
angle. The resin discharge needle fitting unit 73c is made spherical and cylindrical,
a sliding surface 76 on which the resin discharge needle fitting unit 73c can rotate
or be rotatable is provided on the resin discharge unit holding ring 78 of the head
portion 7, and the resin discharge needle fitting unit 73c is provided. Thereby, an
angle of the resin discharge needle 73a can be easily adjusted and it becomes capable
of adjusting the angle of the resin discharge unit 73 without concern for dropout
of the resin discharge needle 73a.
[0037] Regarding the gas ejection hole 71 and the resin discharge unit 73, as shown in
the drawings, the gas ejection hole 71 is provided in a downstream side from the resin
discharge unit 73. According to this structure, the molten resin is gradually elongated
along with a distribution of ejected gas flow ejected from the gas ejection hole 71,
and a fiber having nanometer-order is obtained. By using the heating unit not shown
in the drawings, gas is ejected from the gas piping unit 8 as a hot air. Accordingly,
the resin discharged from the resin discharge unit 73 has a nanofiber larger in length
and smaller in fiber diameter in comparison with the case the normal temperature gas
is ejected.
[0038] Description will be made of a series of operation of the nanofiber producing apparatus
1 having the above structure. the raw material (the resin) fed into the hopper 2 is
melted in the heating cylinder 3 by heating by the heater 4, and sent to a front part
of the heating cylinder 3 by a screw rotated by the motor 6. The molten resin arrived
at the end of the heating cylinder 3 is discharged from the raw material discharge
holes of six resin discharge needles 73 through six resin flow passages 75 provided
in the inside of the head portion 7. The discharged molten resin is carried along
with an air current generated by the high-pressure and high-temperature gas supplied
from the gas piping unit 8 and ejected from the gas ejection hole 71. The nanofiber
is formed by elongating the molten resin by the difference in velocity between rapid
air current of the high-temperature gas and slow air retained therearound.
Embodiment 2
[0039] According to the embodiment 1 of the present invention, detailed description of the
nanofiber producing apparatus was made in which the granular synthetic resin having
a fine particle is melted and used as a raw material. As mentioned before, the liquid
raw material of the nanofiber is not limited thereto, and a dissolved raw material
may be used, which is prepared by dissolving the solid or liquid raw material in the
predetermined solvent in advance so as to obtain the predetermined concentration.
This is also called as the liquid raw material. Figs. 8 to 10 show the nanofiber producing
apparatus for forming the nanofiber from the dissolved raw material. Same reference
numerals are used to the structure same as that in the embodiment 1.
[0040] According to the embodiment 2 of the present invention, a solvent storage unit 5A
is used having function for extruding the dissolved raw material with the predetermined
pressure instead of using the hopper 2, the screw 5 and the motor 6 of the embodiment
1. The gravity caused by difference in height may be applied as the predetermined
pressure. The head portion 7A is connected to a solvent supplying hose 3A and the
gas piping unit 8. The unit for ejecting gas (illustration omitted) may be provided
in the gas piping unit 8 or be introduced from the high-pressure gas supply unit (not
shown) to the gas piping unit 8. As shown in Fig. 9, the head portion 7A is provided
with a gas flow passage 72A and a gas ejection hole 71A as a flow passage of the gas
supplied from the gas piping unit 8. In a similar manner, the head portion 7A is provided
with a resin flow passage 75A as the flow passage of the dissolved raw material, and
the resin flow passage 75A is connected to the resin discharge unit 73. In a similar
manner in the embodiment 1, the resin discharge unit 73 comprises the resin discharge
needles 73a as a discharge hole of the dissolved raw material and the resin discharge
needle fitting unit not shown in Figs. 8 to 10. The head portion 7A is provided with
the resin discharge unit holding ring 78A. By providing the holding adjusting unit
74 comprising he resin discharge needle gripping unit 74a and the adjusting unit 74b
having the adjusting pestle 74c which is retractable and provided penetrating from
outside to inside of the head portion 7A, the discharge angle of the resin discharge
needle 73a can be adjustable at all by the holding adjusting unit 74 as same in the
embodiment 1.
[0041] The nanofiber producing apparatus according to the embodiment 2 is, as shown in Fig.
10, provided with two resin discharge units 73. The number of resin discharge unit
73 is not limited to two, and three or more resin discharge units 73 can be equally
provided around the gas ejection holes 71A. In this case, the resin discharge unit
73 is preferably equally provided. The embodiment in the drawings shows a horizontal
ejection type, however, those skilled in the art can easily consider variations for
ejecting vertically (from upward to downward, or from downward to upward) in a vertical
direction from the gas ejection hole 71A to the gas flow passage 72A.
[0042] In comparison with the structure of the embodiment 1, according to the present embodiment,
the dissolved raw material is used which the raw material is dissolved in the solvent,
and the nanofiber producing apparatus can be composed without using a complicated
component, such as the heating cylinder, the motor, the screw and so on. Thereby,
the apparatus becomes small in size and space can be saved. Additionally, since the
apparatus becomes small in size, a portable nanofiber producing apparatus can be obtained.
In such a portable apparatus, the nanofiber can be formed by spraying the nanofiber
to an area where the nanofiber should be attached, and use of a fiber can be expanded.
[0043] Though description was made of the embodiments of the present invention in detail,
the present invention is not limited to the prescribed embodiments, and various modifications
may be possible within a scope of the present invention. For example, in the above
embodiment, the horizontal nanofiber producing apparatus is described which the molten
resin and the gas ejection hole are provided in a horizontal direction, however it
is not limited thereto, there is no problem to arrange the vertical apparatus and
method for producing the nanofiber in the downward. If we adopt the vertical apparatus
and method, an effect of gravity can be effectively prevented. The extruding unit
is explained as the screw 5, however as a die cast method, there is no problem if
the solvent is supplied in order and intermittent extrusion is made by using a piston,
although countermeasures should be taken against interruption of produced nanofiber.
Furthermore, the gas ejection hole 71 may be nozzle shape by forming in a taper shape
so as to increase the pressure thereof. Two examples are raised and described about
the structure of adjusting the angles of the resin discharge needle 73a, however,
there can be applied the structure capable of adjusting the angles of the bellows-type
resin discharge unit and so on.
- 1
- nanofiber producing apparatus
- 2
- hopper
- 3
- heating cylinder
- 4
- heater
- 5
- screw
- 6
- motor
- 7
- head portion
- 71
- gas ejection unit
- 72
- gas flow passage
- 73
- resin discharge unit
- 73a
- resin discharge needle
- 73b, 73c
- resin discharge needle fitting unit
- 74
- holding adjusting unit
- 74a
- resin discharge needle gripping unit
- 74b
- adjusting unit
- 74c
- adjusting pestle
- 75
- resin flow passage
- 76
- sliding surface
- 77
- heating cylinder cover unit
- 78
- resin discharge unit holding ring
- 8
- gas piping unit
- 81
- pipe
- 90
- high-pressure gas flow
- 91
- central line
1. An apparatus (1) for producing a nanofiber, comprising:
a high-pressure gas ejection unit (71) for ejecting a high-pressure gas flow (90);
and
a plurality of liquid raw material discharge units (73) for discharging a liquid raw
material to the high-pressure gas flow (90) ejected from said high-pressure gas ejection
unit (71), wherein
said liquid raw material discharge units (73) are provided around a center of the
high-pressure gas flow (90) ejected from said high-pressure gas ejection unit (71),
characterized by
an angle adjustment unit (74) capable of adjusting an installation angle (θ) of said
liquid raw material discharge units (73) to the high-pressure gas flow (90) ejected
from said high-pressure gas ejection unit (71).
2. An apparatus (1) for producing the nanofiber according to claim 1, wherein said liquid
raw material discharge units (73) are provided with an extruding unit (5) for melting
and extruding a raw material, and said liquid raw material discharge units (73) discharge
the raw material melted and extruded by said extruding unit (5) as the liquid raw
material.
3. An apparatus (1) for producing the nanofiber according to claim 1, wherein said liquid
raw material discharge units (73) are provided with a unit (5A) for supplying dissolved
raw material, and said liquid raw material discharge units (73) discharge the dissolved
raw material as the liquid raw material.
4. An apparatus (1) for producing the nanofiber according to any one of claims 1 to 3,
wherein said high-pressure gas ejection unit (71) is provided with a gas supply unit
for supplying a high-pressure and high-temperature gas, and said high-pressure gas
ejection unit (71) ejects said high-pressure and high-temperature gas as the high-pressure
gas flow (90).
5. An apparatus (1) for producing the nanofiber according to any one of claims 1 to 4,
wherein at least two or more of said liquid raw material discharge units (73) are
symmetrically provided to said high-pressure gas ejection unit (71).
6. An apparatus (1) for producing the nanofiber according to any one of claims 1 to 5,
wherein said liquid raw material discharge units (73) are provided at equal intervals
around the high-pressure gas flow (90) ejected from said high-pressure gas ejection
unit (71).
7. An apparatus (1) for producing the nanofiber according to any one of claims 1 to 6,
wherein the high-pressure gas flow (90) ejected from said high-pressure gas ejection
unit (71) is provided in a vertical direction to an installation surface of the apparatus
(1).
8. A method for producing a nanofiber by using an apparatus (1) for producing the nanofiber
according to any one of claims 1 to 7, wherein
a high-pressure gas flow (90) is ejected from said high-pressure gas ejection unit
(71),
a liquid raw material is discharged from said liquid raw material discharge units
(73) to the high-pressure gas flow (90) ejected from said high-pressure gas ejection
unit (71), and
a discharge angle (θ) of the liquid raw material discharged from said liquid raw material
discharge units (73) to said high-pressure gas flow (90) is adjusted using said angle
adjustment unit (74), when said liquid raw material discharge units (73) discharge
the liquid raw material to the high-pressure gas flow (90) as a center.
9. A method for producing a nanofiber using a nanofiber producing apparatus (1) comprising
a heating cylinder (3) to which a raw material is fed, a heating unit (4) for heating
the heating cylinder (3), and an extruding unit (5) for extruding the raw material
in said heating cylinder (3), wherein,
an end portion of said heating cylinder (3) is provided with a gas ejection hole (71)
for ejecting a high-pressure gas,
a plurality of raw material discharge units (73) for discharging the raw material
in melting state in said heating cylinder (3) are provided around said gas ejection
hole (71), and
a fiber having nanometer-order diameter is obtained by heating said heating cylinder
(3) by said heating unit (4), by melting the raw material supplied in said heating
cylinder (3) or being maintained in a melting state, by extruding the raw material
from said extruding unit (5) and discharging from said raw material discharge units
(73), by generating an air current by the gas ejected from said gas ejection hole
(71), and by carrying and elongating said discharged raw material along with the air
current of the ejected gas from the periphery.
1. Vorrichtung (1) zur Herstellung einer Nanofaser, umfassend:
eine Ausstoßeinheit für Hochdruckgas (71) zum Ausstoßen eines Hochdruckgasstroms (90);
und
mehrere Austragseinheiten für flüssiges Rohmaterial (73) zum Austragen eines flüssigen
Rohmaterials in den Hochdruckgasstrom (90), der aus der Ausstoßeinheit für Hochdruckgas
(71) ausgestoßen wird, wobei
die Austragseinheiten für flüssiges Rohmaterial (73) um einen Mittelpunkt des Hochdruckgasstroms
(90), der aus der Ausstoßeinheit für Hochdruckgas (71) ausgestoßen wird, vorgesehen
sind,
gekennzeichnet durch
eine Einheit zum Einstellen des Winkels (74), die in der Lage ist, einen Installationswinkel
(θ) der Austragseinheiten für flüssiges Rohmaterial (73) in den Hochdruckgasstrom
(90), der aus der Ausstoßeinheit für Hochdruckgas (71) ausgestoßen wird, einzustellen.
2. Vorrichtung (1) zur Herstellung der Nanofaser gemäß Anspruch 1, wobei die Austragseinheiten
für flüssiges Rohmaterial (73) mit einer Extrudiereinheit (5) zum Schmelzen und Extrudieren
eines Rohmaterials versehen sind und die Austragseinheiten für flüssiges Rohmaterial
(73) das durch die Extrudiereinheit (5) geschmolzene und extrudierte Rohmaterial als
das flüssige Rohmaterial abgeben.
3. Vorrichtung (1) zur Herstellung der Nanofaser gemäß Anspruch 1, wobei die Austragseinheiten
für flüssiges Rohmaterial (73) mit einer Einheit (5A) zum Zuführen von gelöstem Rohmaterial
versehen sind und die Austragseinheiten für flüssiges Rohmaterial (73) das gelöste
Rohmaterial als das flüssige Rohmaterial abgeben.
4. Vorrichtung (1) zur Herstellung der Nanofaser gemäß einem der Ansprüche 1 bis 3, wobei
die Ausstoßeinheit für Hochdruckgas (71) mit einer Gaszuführeinheit zum Zuführen eines
Hochdruck- und Hochtemperaturgases versehen ist und die Ausstoßeinheit für Hochdruckgas
(71) das Hochdruck- und Hochtemperaturgas als den Hochdruckgasstrom (90) ausstößt.
5. Vorrichtung (1) zur Herstellung der Nanofaser gemäß einem der Ansprüche 1 bis 4, wobei
mindestens zwei oder mehr der Austragseinheiten für flüssiges Rohmaterial (73) symmetrisch
zu der Ausstoßeinheit für Hochdruckgas (71) vorgesehen sind.
6. Vorrichtung (1) zur Herstellung der Nanofaser gemäß einem der Ansprüche 1 bis 5, wobei
die Austragseinheiten für flüssiges Rohmaterial (73) in gleichen Abständen um den
Hochdruckgasstrom (90), der aus der Ausstoßeinheit für Hochdruckgas (71) ausgestoßen
wird, vorgesehen sind.
7. Vorrichtung (1) zur Herstellung der Nanofaser gemäß einem der Ansprüche 1 bis 6, wobei
der Hochdruckgasstrom (90), der aus der Ausstoßeinheit für Hochdruckgas (71) ausgestoßen
wird, in einer vertikalen Richtung zu einer Installationsoberfläche der Vorrichtung
(1) vorgesehen ist.
8. Verfahren zur Herstellung einer Nanofaser durch Verwendung einer Vorrichtung (1) zur
Herstellung der Nanofaser gemäß einem der Ansprüche 1 bis 7, wobei
ein Hochdruckgasstrom (90) aus der Ausstoßeinheit für Hochdruckgas (71) ausgestoßen
wird,
ein flüssiges Rohmaterial von den Austragseinheiten für flüssiges Rohmaterial (73)
in den Hochdruckgasstrom (90), der aus der Ausstoßeinheit für Hochdruckgas (71) ausgestoßen
wird, ausgetragen wird und
ein Austragswinkel (θ) des flüssigen Rohmaterials, das von den Austragseinheiten für
flüssiges Rohmaterial (73) in den Hochdruckgasstrom (90) ausgetragen wird, unter Verwendung
der Einheit zum Einstellen des Winkels (74) eingestellt wird, wenn die Austragseinheiten
für flüssiges Rohmaterial (73) das flüssige Rohmaterial in den Hochdruckgasstrom (90)
als Mittelpunkt austragen.
9. Verfahren zur Herstellung einer Nanofaser durch Verwendung einer Nanofasern herstellenden
Vorrichtung (1), umfassend einen Heizzylinder (3), zu dem ein Rohmaterial zugeführt
wird, eine Heizeinheit (4) zum Heizen des Heizzylinders (3) und eine Extrudiereinheit
(5) zum Extrudieren des Rohmaterials in dem Heizzylinder (3), wobei
ein Endbereich des Heizzylinders (3) mit einem Gasausstoßloch (71) zum Ausstoßen eines
Hochdruckgases versehen ist,
mehrere Austragseinheiten für Rohmaterial (73) zum Austragen des Rohmaterials in einem
geschmolzenen Zustand in dem Heizzylinder (3) um das Gasausstoßloch (71) vorgesehen
sind, wobei
eine Faser, die einen Durchmesser in der Nanometer-Größenordnung aufweist, durch Erhitzen
des Heizzylinders (3) mittels der Heizeinheit (4), durch Schmelzen des zugeführten
Rohmaterials in dem Heizzylinder (3) oder durch Halten in einem geschmolzenen Zustand,
durch Extrudieren des Rohmaterials aus der Extrudiereinheit (5) und Austragen desselben
aus den Austragseinheiten für Rohmaterial (73), durch Erzeugen eines Luftstroms durch
das aus dem Gasausstoßloch (71) ausgestoßene Gas und durch Befördern und Strecken
des ausgetragenen Rohmaterials zusammen mit dem Luftstrom des ausgestoßenen Gases
von der Peripherie erhalten wird.
1. Appareil (1) destiné à la production d'une nanofibre comprenant :
une unité d'éjection de gaz à haute pression (71) permettant d'éjecter un flux de
gaz à haute pression (90) ; et
une pluralité d'unités de décharge de matière première liquide (73) permettant de
décharger une matière première liquide vers le flux de gaz à haute pression (90) éjecté
depuis ladite unité d'éjection du gaz à haute pression (71), dans lequel
lesdites unités de décharge de matière première liquide (73) sont disposées autour
d'un centre du flux de gaz à haute pression (90) éjecté depuis ladite unité d'éjection
du gaz à haute pression (71),
caractérisé par
une unité de réglage d'angle (74) capable d'ajuster un angle d'installation (θ) desdites
unités de décharge de matière première liquide (73) vers le flux de gaz à haute pression
(90) éjecté depuis ladite unité d'éjection de gaz à haute pression (71).
2. Appareil (1) destiné à la production d'une nanofibre selon la revendication 1, dans
lequel lesdites unités de décharge de matière première liquide (73) sont munies d'une
unité d'extrusion (5) permettant la fonte et l'extrusion de matière première, et lesdites
unités de décharge de matière première liquide (73) déchargent la matière première
fondue et extrudée par lesdites unités d'extrusion (5) en tant que matière première
liquide.
3. Appareil (1) destiné à la production d'une nanofibre selon la revendication 1, dans
lequel lesdites unités de décharge de matière première liquide (73) sont équipées
d'une unité (5A) permettant la fourniture de matière première dissoute, et lesdites
unités de décharge de matière première liquide (73) déchargent la matière première
dissoute en tant que matière première liquide.
4. Appareil (1) destiné à la production d'une nanofibre selon l'une quelconque des revendications
1 à 3, dans lequel ladite unité d'éjection de gaz à haute pression (71) est équipée
d'une unité de fourniture de gaz permettant de fournir un gaz à haute pression et
à haute température, et ladite unité d'éjection de gaz à haute pression (71) éjecte
ledit flux de gaz à haute pression et à haute température en tant que flux de gaz
à haute pression (90).
5. Appareil (1) destiné à la production d'une nanofibre selon l'une quelconque des revendications
1 à 4, dans lequel au moins deux ou plusieurs unités de décharge de matière première
liquide (73) sont disposées de manière symétrique par rapport à ladite unité d'éjection
de gaz à haute pression (71).
6. Appareil (1) destiné à la production d'une nanofibre selon l'une quelconque des revendications
1 à 5, dans lequel lesdites unités de décharge de matière première liquide (73) sont
disposées à des intervalles égaux autour du flux de gaz à haute pression (90) éjecté
depuis ladite unité d'éjection de gaz haute pression (71).
7. Appareil (1) destiné à la production d'une nanofibre selon l'une quelconque des revendications
1 à 6, dans lequel le flux de gaz à haute pression (90) éjecté depuis ladite unité
d'éjection de gaz à haute pression (71) est disposé dans une direction verticale à
une surface d'installation de l'appareil (1).
8. Procédé de production d'une nanofibre par l'utilisation d'un appareil (1) destiné
à la production de la nanofibre selon l'une quelconque des revendications 1 à 7, dans
lequel
un flux de gaz à haute pression (90) est éjecté depuis ladite unité d'éjection de
gaz à haute pression (71),
une matière première liquide est déchargée à partir desdites unités de décharge de
matière première liquide (73) vers le flux de gaz à haute pression (90) éjecté depuis
ladite unité d'éjection de gaz à haute pression (71), et
un angle de décharge (θ) de la matière première liquide déchargée provenant desdites
unités de décharge de matière première liquide (73) vers ledit flux de gaz à haute
pression (90) est ajusté en utilisant ladite unité de réglage d'angle (74), lorsque
lesdites unités de décharge de matière première liquide (73) déchargent la matière
première liquide vers le flux de gaz à haute pression (90) en tant que centre.
9. Procédé de production d'une nanofibre en utilisant un appareil de production de nanofibres
(1) comprenant un cylindre de chauffage (3) auquel une matière première est alimentée,
une unité de chauffage (4) destinée au chauffage du cylindre de chauffage (3), et
une unité d'extrusion (5) permettant d'extruder la matière première dans ledit cylindre
de chauffage (3), dans lequel,
une partie d'extrémité du cylindre de chauffage (3) est équipée d'un trou d'éjection
de gaz (71) permettant d'éjecter un gaz à haute pression,
une pluralité d'unités de décharge matières première (73) permettant de décharger
la matière première dans un état fondu dans ledit cylindre de chauffage (3) sont montées
autour dudit trou d'éjection de gaz (71), et
une fibre ayant un diamètre de l'ordre du nanomètre est obtenue par chauffage dudit
cylindre de chauffage (3) au moyen de ladite unité de chauffage (4), par fonte de
la matière première fournie dans ledit cylindre de chauffage (3) ou étant maintenue
dans un état fondu, par extrusion de la matière première à partir de ladite unité
d'extrusion (5) et par déchargement à partir desdits unités de décharge de matières
premières (73), par génération d'un courant d'air au moyen du gaz éjecté à partir
dudit trou d'éjection de gaz (71), et par portée et élongation de ladite matière première
déchargée accompagné du courant d'air du gaz éjecté provenant de la périphérie.