The present invention relates to a microwave heating unit that heats a continuous fiber as a heating subject by irradiating the fiber with microwaves, to the fiber and a method for producing a carbon fiber using the microwave heating unit.
Carbon fibers have excellent specific strength and specific elastic modulus as compared with other fibers, and are widely used industrially as reinforcing fibers to be combined with a resin or the like by utilizing their lightweight properties and excellent mechanical properties.
Conventionally, carbon fibers are produced as follows. First, a precursor fiber is subjected to a flame resistance treatment by being heated in a heating air at 230° C. to 260° C. inclusive for 30 minutes to 100 minutes inclusive. By this flame resistance treatment, a cyclization reaction of an acrylic fiber is caused to increase the amount of oxygen bonding, thereby obtaining a flame-resistant fiber. The flame-resistant fiber is carbonized with a temperature gradient using a pyrolyzing furnace at 300° C. to 800° C. inclusive in a nitrogen atmosphere, for example (first carbonization treatment). Next, carbonization is further performed with a temperature gradient using the pyrolyzing furnace at 800° C. to 2100° C. inclusive in the nitrogen atmosphere (second carbonization treatment). Thus, a carbon fiber is produced by heating the flame-resistant fiber from the outside of the fiber in the pyrolyzing furnace which has been heated.
In the case of production as described above, in order to avoid insufficient carbonization of the inside of the fibers to be carbonized, the temperature must be gradually increased over time. In addition, in the pyrolyzing furnace in which the fiber is heated from the outside of the fiber, substances other than the fibers to be carbonized, such as a furnace body and a pyrolyzing atmosphere, are also heated, and thus, the thermal efficiency is low.
So far, attempts have been made to produce carbon fibers through heating carbonized fibers to be carbonized by irradiating the fibers with microwaves to the fibers. A substance is heated by microwaves from the inside thereof. Therefore, when fibers to be carbonized is heated using microwaves, carbonization can be uniformly performed on the surface of the fiber and inside the fiber, and a reduction in the production time of the carbon fiber is expected.
Conventionally, Patent Literature 1 is known as a method for producing a carbon fiber using microwaves.
Patent Literature 1 describes a method for producing a carbon fiber using microwaves.
Further, Patent Literature 2 discloses a microwave heating apparatus that suppresses heating unevenness of food or the like by conveying a heating object obliquely with respect to a heating furnace.
However, in the production process of the carbon fiber, the fiber as the heating subject continuously changes from a dielectric to a semiconductor and then to a conductor. In particular, in the production process of the carbon fiber using microwaves, the properties of the heating subject fiber change instantaneously. That is, a change in the dielectric constant of the heating subject fiber causes suitable heating conditions change instantaneously. Therefore, when the heating subject fiber is heated using the conventional microwave heating unit, an unstable reaction tends to occur due to the properties of electromagnetic energy in the furnace, and the heating subject fiber may be significantly damaged, and thus, the process stability may be deteriorated and the quality of the obtained fiber may be significantly deteriorated.
The object of the present invention is to provide a small-sized microwave heating unit that heats a fiber as a heating subject by irradiating microwaves to the fiber and is capable of stably heating the fiber as the heating subject when the dielectric constant of the fiber as the heating subject is changed. Another object of the present invention is to provide a method for producing a carbon fiber, wherein a heating subject fiber is carbonized using the microwave heating unit.
The present inventors have found that the above problem can be solved by causing the heating subject continuous fiber to run obliquely with respect to an axis of the furnace body. That is, it has been found that when the electromagnetic field distribution generated in the furnace body reaches a maximum electric field intensity at predetermined positions of a waveguide, by causing the heating subject continuous fiber to run obliquely with respect to the tube axis of the waveguide, the heating subject continuous fiber is heated in the vicinity of the maximum electric field intensity, and the heating subject continuous fiber whose dielectric constant has been changed by the heating is quickly retracted from the vicinity of the maximum electric field intensity, and thereby, the electric field reflection caused by the change of the continuous fiber as the heating subject into a semiconductor or a conductor can be suppressed and the process stability can be improved.
In addition, it has been found that when heating is performed after the continuous fiber as the heating subject which is a dielectric is changed into a semiconductor or a conductor, heating using an electric field component of a microwave tends to cause severance due to electric discharge, the heating becomes unstable, and the quality of the heating subject continuous fiber is significantly deteriorated, and such a problem can be solved by heating using a magnetic field component.
In addition, the present inventors have conceived that a cylindrical heat insulating tube through which microwaves are transmitted is disposed in a cylindrical furnace body and a heating subject continuous fiber is caused to run in the heat insulating tube to be irradiated with microwaves. It has been found that since the heat insulating tube absorbs microwaves and generates heat by itself at a high temperature, the carbonization rate can be remarkably improved by keeping the heating subject continuous fiber at a high temperature.
The present invention has been completed based on these findings.
The present invention for solving the above-described problem is as described below.
[1] A microwave heating unit (1000, 1000a, 1000b, 1000c, 1001, 1002, 1003, 1004) including:
[2] The microwave heating unit according to [1], wherein the angle θ° satisfies 10<θ<60.
The microwave heating unit of the above-described [1] and [2] uses the waveguide as the furnace body and irradiates the heating subject continuous fiber running inside the waveguide with microwaves under an atmospheric pressure, wherein a fiber as a heating subject is caused to run obliquely with respect to the tube axis of the waveguide.
[3] The microwave heating unit according to [1], wherein the waveguide is a rectangular waveguide, and the fiber inlet and the fiber outlet are respectively provided on a short-side tube wall of the waveguide.
[4] The microwave heating unit according to [1], further including: a heat insulating tube (107, 207, 307) that penetrates the waveguide and connects the fiber inlet and the fiber outlet, wherein the heating subject continuous fiber is configured to run inside the heat insulating tube.
[5] The microwave heating unit according to [1], wherein a material of the heat insulating tube is a ceramic.
In the microwave heating unit of the above-described [4] and [5], an outer periphery of a running portion of the continuous fiber as the heating subject is covered with the heat insulating tube made of ceramic.
[6] A method for producing an intermediate carbon fiber or a carbon fiber, the method heating a continuous fiber as a heating subject while causing the continuous fiber as the heating subject to run using the microwave heating unit according to any one of [1] to [5], and the method including a process of heating a continuous fiber as a heating subject having a carbon content of less than 66% by mass to obtain an intermediate carbon fiber or a carbon fiber.
[7] The method according to [6], wherein a continuous fiber as a heating subject is further heated by a maximum magnetic field portion in a waveguide while being caused to run using the microwave heating unit according to any one of [1] to [5].
The method according to any one of the above-described [6] and [7] is a method for producing a carbon fiber using the microwave heating unit according to any one of [1] to [5] in at least a part of a carbon fiber production process.
In the microwave heating unit of the present invention, the heating subject continuous fiber runs obliquely with respect to the axis of the furnace body. Therefore, the continuous fiber as the heating subject which is heated at the maximum electric field portion in the furnace body and changed in property (dielectric constant) can be quickly retracted from the maximum electric field portion. As a result, electric field reflection due to the fiber that has become a semiconductor or a conductor in the furnace is less likely to occur, and the process stability can be improved.
When a rectangular waveguide is used as the furnace body and the fiber inlet and the fiber outlet are loaded on the H-plane of the rectangular waveguide, the width of the furnace body can be reduced and the apparatus can be made compact.
Further, when the heat insulating tube is used, the continuous fiber as the heating subject can be maintained at a high temperature, and thus, the efficiency of carbonization can be improved.
Hereinafter, a microwave heating unit and a method for producing a carbon fiber using the microwave heating unit according to the present invention will be described in detail with reference to the drawings.
In the present invention, the H-plane of the furnace body refers to a short-side tube wall of a rectangular waveguide, and the E-plane of the furnace body refers to a long-side tube wall of the rectangular waveguide.
In the present invention, dielectric, semiconductor and conductor are not distinguished by clear numerical values, and mean that a continuous fiber as a heating subject in a state before being heated is a dielectric, the continuous fiber as the heating subject in a completely heated state is a conductor, and the continuous fiber as the heating subject in an intermediate state therebetween is a semiconductor. That is, when the continuous fiber as the heating subject is a carbon fiber precursor, it means that a carbon fiber precursor (having a carbon content of 66% to 72% inclusive by mass) is a dielectric, a carbon fiber or graphitized fiber is a conductor (having a carbon content of 90% by mass or more), and an intermediate state therebetween is a semiconductor.
(1) Microwave Heating Unit
(2) Furnace Body
The furnace body 100 of the microwave heating unit of the present invention includes a cylindrical waveguide or a rectangular waveguide. By introducing the microwave into the waveguide, an electromagnetic field distribution of a TE (Transverse Electric) mode is formed in the waveguide. A TE mode refers to a transmission mode having an electric field component orthogonal to the direction of the microwave transmitted in the waveguide. By generating a standing wave in the furnace body 100, a place where an electric field component reaches the maximum and a place where a magnetic field component reaches the maximum are present at different positions in the furnace body 100. Therefore, by causing the continuous fiber as the heating subject to run in the furnace body, heating mainly by an electric field component (hereinafter also referred to as “electric field heating”) and heating mainly by a magnetic field component (hereinafter also referred to as “magnetic field heating”) may be respectively performed.
(2-1) Furnace Body Using Cylindrical Waveguide
In
Next, the operation of the microwave heating unit 1000 will be described. In
The angle θ° between the tube axis of the furnace body 101 and the tube axis of the heat insulating tube 107 is 0<θ<90, preferably 10<θ<60, and more preferably 15<θ<55. It is configured that the continuous fiber as the heating subject 150 is carried out of the furnace body from a portion other than the terminal end portion of the furnace body. That is, the fiber outlet 105 is formed on the outer peripheral surface along the tube axis of the furnace body 101. By obliquely intersecting the tube axis of the furnace body 101 with the tube axis of the heat insulating tube 107, the running direction of the continuous fiber as the heating subject is inclined with respect to the tube axes, and thus, while running in the maximum electric field portion or the maximum magnetic field portion, the continuous fiber as the heating subject can be prevented from running only in the maximum electric field portion or the maximum magnetic field portion. As a result, the process stability can be improved as described below. The angle θ° between the tube axis of the furnace body 101 and the continuous fiber as the heating subject 150 is 0<θ<90, preferably 10<θ<60, and more preferably 15<θ<55.
(2-2) Furnace Body Using Rectangular Waveguide
(a) H-Plane Loading Furnace
Next, the operation of the microwave heating unit 1001 will be described. In
The angle θ° between the tube axis of the furnace body 201 and the tube axis of the heat insulating tube 207 is 0<θ<90, preferably 10<θ<60, and more preferably 15<θ<55. It is configured that the continuous fiber as the heating subject 250 is carried out of the furnace body from a portion other than the terminal end portion of the furnace body. That is, the fiber outlet 205 is formed on the H-plane 201b of the furnace body 201. By obliquely intersecting the tube axis of the furnace body 201 with the tube axis of the heat insulating tube 207, the running direction of the heating subject continuous fiber is inclined with respect to the tube axes, and thus, while running in the maximum electric field portion or the maximum magnetic field portion, the heating subject continuous fiber can be prevented from running only in the maximum electric field portion or the maximum magnetic field portion. As a result, the process stability can be improved as described below. The angle θ° between the tube axis of the furnace body 201 and the continuous fiber as the heating subject 250 is 0<θ<90, preferably 10<θ<60, and more preferably 15<θ<55.
In the present invention, it is preferable that the furnace is an H-plane loading furnace capable of reducing a machine width and an equal pitch.
(b) E-Plane Loading Furnace
Since the operation of the microwave heating unit 1002 is the same as that of the above-described microwave heating unit 1001, the description thereof is omitted.
(3) Electric Field Heating
Hereinafter, a configuration of a furnace body for heating the carbon fiber precursor which is a dielectric by electric field heating will be described.
(4) Magnetic Field Heating
Hereinafter, the configuration of a furnace body for heating the continuous fiber as the heating subject which is a semiconductor or a conductor by magnetic field heating will be described.
(5) Heat Insulating Tube
It is preferable that the microwave heating unit of the present invention includes a heat insulating tube. The heat insulating tube is inserted into the furnace body in a manner of penetrating the furnace body and connecting the fiber inlet and the fiber outlet, wherein the heating subject continuous fiber is capable of running inside the heat insulating tube. The heat insulating tube keeps the inside of the tube at a high temperature by blocking the radiant heat generated by the heating of the heating subject continuous fiber and thereby suppressing heat dissipation. The inside of the heat insulating tube is at the normal pressure and is in the inert atmosphere supplied by the inert gas supply means which is not illustrated.
It is preferable that the heat insulating tubes 107, 207, 307 are cylindrical. The inner diameters of the heat insulating tubes 107, 207, 307 are not particularly limited, but are generally 8 mm to 55 mm inclusive. The outer diameters of the heat insulating tubes 107, 207, 307 are not particularly limited, but are generally 10 mm to 60 mm inclusive. The lengths of the heat insulating tubes 107, 207, 307 are not particularly limited, but are generally 100 mm to 2500 mm inclusive. In addition, the material of the heat insulating tubes 107, 207, 307 needs to be a material that transmits microwaves, and the transmittance of microwaves is preferably 90% to 100% inclusive and more preferably 95% to 100% inclusive at room temperature (25° C.). Examples of such a material include a ceramic of quartz, alumina, etc. The microwave transmittances of these materials are 100% for quartz and 99.9% for alumina, respectively. The microwave transmittances of the ceramics vary depending on the composition, and the microwave transmittance is 99.9% in the case of silica 41%-alumina 55%, but the composition is not limited to this combination as long as the microwave transmittance is within the above-described range. The ceramic may contain metal oxides such as alumina, silica-alumina, titania, zirconia, magnesia, and calcia; metal nitrides such as silicon nitride, aluminum nitride, and titanium nitride; and other compounds. In particular, alumina or silica-alumina is preferable because alumina or silica-alumina functions as a susceptor that absorbs a part of microwaves and generates heat at a high temperature. At both ends of each of the heat insulating tubes 107, 207, 307, a material which absorbs microwaves may be provided to prevent microwave leakage.
The shape of the waveguide used as the furnace body is not particularly limited as long as an electromagnetic field distribution of the TE mode can be formed in the waveguide. In general, it is preferable that the length of the waveguide is 500 mm to 1500 mm inclusive. It is preferable that the opening of the cross section orthogonal to the tube axis of the rectangular waveguide has a long side of 105 mm to 115 mm inclusive and a short side of 50 mm to 60 mm inclusive. The material of the waveguide is not particularly limited, but is generally made of a metal such as stainless steel, iron, copper, or aluminum.
The frequency of the microwaves is not particularly limited, but generally 915 MHz, 2.45 GHz or 5.8 GHz is used. The output of the microwave oscillator is not particularly limited, but is suitably 300 W to 2400 W inclusive, and more suitably 500 W to 2000 W inclusive.
The conveying speed of a fiber to be carbonized in a carbonization furnace is preferably 0.05 m/min to 10 m/min inclusive, more preferably 0.1 m/min to 5.0 m/min inclusive, and particularly preferably 0.2 m/min to 2.0 m/min inclusive.
The carbon fiber thus obtained has a carbon content of preferably 90% by mass or more, more preferably 91% by mass or more.
(6) Method for Producing Carbon Fiber
When a carbon fiber is produced using the microwave heating unit of the present invention, a plurality of the microwave heating units of the present invention can be connected in series to perform heating. Further, a microwave heating unit other than the microwave heating unit of the present invention may be included, or a heating device other than a microwave heating unit may be included.
Hereinafter, the present invention will be described in more detail with reference to examples. The present invention is not limited to these examples.
In the following examples, the carbon fiber precursor fiber refers to a PAN-based flame-resistant fiber having a carbon content of 60% by mass, and the intermediate carbon fiber refers to a PAN-based intermediate carbon fiber having a carbon content of 66% by mass unless otherwise specified. “Processability” is evaluated as E when the single filament can be continuously carbonized (continuous operation) without breaking, as “o” when a part of the single filament is broken but the continuous operation is possible, as “A” when the single filament is broken and the broken single filament is thus entangled with a conveying device such as a roll and easily hinders the continuous operation, and as “x” when the entire fiber bundle is broken and cannot be taken out from the furnace body. “Fiber quality” is evaluated as “E” when the fiber is not broken at all during carbonization, as “o” when a very small amount of fluff is generated on the fiber during carbonization, as “A” when a large amount of fluff is generated, and as “x” when the fiber is completely broken.
The microwave heating unit described in
Microwaves are introduced into the furnace body in a nitrogen gas atmosphere to form the electromagnetic field distribution of the TE mode. The output of the microwave oscillator is configured to be 300 W. A carbon fiber precursor is carbonized while being caused to run at 0.3 m/min in a manner that the carbon fiber precursor which is a dielectric and the maximum electric field portion in the furnace body intersect at the axis of the furnace body to obtain a carbon fiber. The carbon content of the obtained carbon fiber is 93% by mass, no breakage of the fiber is found, and the processability is extremely good. The evaluation results are illustrated in Table 1.
An intermediate carbon fiber is obtained by heating in the same manner as in Example 1 except that the angle between the axis of the furnace body and the fiber running direction is changed to 54°. At this time, the length of the fiber housed in the furnace body is 136 mm. Although some single filaments are found broken during the process, the processability is good. The evaluation results are illustrated in Table 1.
An intermediate carbon fiber is obtained by heating in the same manner as in Example 1 except that the angle between the axis of the furnace body and the fiber running direction is changed to 17° and the length of the heat insulating tube is changed to 500 mm. At this time, the length of the fiber housed in the furnace body is 376 mm. Although the temperature of the furnace has risen, during the process, it does not reach a temperature sufficient for the carbonization reaction of the fiber, and the intermediate carbon fiber and carbon fiber cannot be obtained. The evaluation results are illustrated in Table 1.
The microwave heating unit described in
The microwave heating unit described in
A carbon fiber is obtained by heating in the same manner as in Example 1 except that the carbon fiber precursor and the maximum magnetic field portion in the furnace body are changed to intersect at the axis of the furnace body. At this time, the length of the fiber housed in the furnace body is 183 mm. The carbon content of the obtained carbon fiber is 93% by mass, no breakage of the fiber is found, and the processability is extremely good. The evaluation results are illustrated in Table 1.
An intermediate carbon fiber is obtained by heating in the same manner as in Example 4 except that the angle between the axis of the furnace body and the fiber running direction is changed to 54°. At this time, the length of the fiber housed in the furnace body is 136 mm. The carbon content of the obtained intermediate carbon fiber is 70% by mass, and although some single yarns are found broken during the process, the processability is good. The evaluation results are illustrated in Table 1.
An intermediate carbon fiber is obtained by heating in the same manner as in Example 4 except that the angle between the axis of the furnace body and the fiber running direction is changed to 17° and the length of the heat insulating tube is changed to 500 mm. At this time, the length of the fiber housed in the furnace body is 376 mm. Although the temperature of the furnace has risen, during the process, the temperature rise is not sufficient for the carbonization reaction of the fiber, and the intermediate carbon fiber and carbon fiber cannot be obtained. The evaluation results are illustrated in Table 1.
The heating is performed in the same manner as in Comparative Example 2 except that the carbon fiber precursor and the maximum magnetic field portion in the furnace body are changed to intersect at the axis of the furnace body (that is, the configuration of
An intermediate carbon fiber is obtained by heating in the same manner as in Example 1 except that the fiber inlet and fiber outlet are loaded on the E-plane of the furnace body (that is, the configuration of
An intermediate carbon fiber is obtained by heating in the same manner as in Example 7 except that the angle between the axis of the furnace body and the fiber running direction is changed to 54°. At this time, the length of the fiber housed in the furnace body is 68 mm. The carbon content of the obtained intermediate carbon fiber is 72% by mass, some single yarns are found broken, and the heating subject fiber tends to wind around a conveying roll. The evaluation results are illustrated in Table 1.
An intermediate carbon fiber is obtained by heating in the same manner as in Example 7 except that the angle between the axis of the furnace body and the fiber running direction is changed to 17°. At this time, the length of the fiber housed in the furnace body is 188 mm. No breakage of the fiber is found, and the processability is extremely good. The evaluation results are illustrated in Table 1.
As in the configuration illustrated in
An intermediate carbon fiber is obtained by heating in the same manner as in Example 7 except that the carbon fiber precursor and the maximum electric field portion in the furnace body are changed to intersect at the axis of the furnace body. At this time, the length of the fiber housed in the furnace body is 91 mm. The carbon content of the obtained intermediate carbon fiber is 72%, no breakage of the fiber is found, and the processability is extremely good. The evaluation results are illustrated in Table 1.
An intermediate carbon fiber is obtained by heating in the same manner as in Example 10 except that the angle between the axis of the furnace body and the fiber running direction is changed to 54°. At this time, the length of the fiber housed in the furnace body is 68 mm. Some single yarns are found broken during the process, and the fiber as the heating subject tends to wind around the conveying roll. The evaluation results are illustrated in Table 1.
An intermediate carbon fiber is obtained by heating in the same manner as in Example 10 except that the angle between the axis of the furnace body and the fiber running direction is changed to 17°. At this time, the length of the fiber housed in the furnace body is 188 mm. No breakage of the fiber is found, and the processability is extremely good. The evaluation results are illustrated in Table 1.
The heating is performed in the same manner as in Comparative Example 4 except that the maximum electric field portion in the furnace body and the carbon fiber precursor are changed to intersect at the axis of the furnace body (that is, the configuration of
A carbon fiber is obtained by carbonizing in the same manner as in Example 4 except that the fiber to be heated is changed from the carbon fiber precursor to an intermediate carbon fiber which is a semiconductor or a conductor. The carbon content of the obtained carbon fiber is 95% by mass, no breakage of the fiber is found, and the processability is extremely good. The evaluation results are illustrated in Table 2.
A carbon fiber is obtained by heating in the same manner as in Example 13 except that the angle between the axis of the furnace body and the fiber running direction is changed to 54°. The length of the fiber housed in the furnace body is 136 mm. Some single filaments are found broken, and the heating subject fiber tends to wind around the conveying roll. The evaluation results are illustrated in Table 2.
A carbon fiber is obtained by heating in the same manner as in Example 13 except that the angle between the axis of the furnace body and the fiber running direction is changed to 17°. The length of the fiber housed in the furnace body is 376 mm. Although some filaments are found broken during the process, the processability is good. The evaluation results are illustrated in Table 2.
Carbonization is performed in the same manner as in Comparative Example 1 except that the fiber to be heated is changed from the carbon fiber precursor to an intermediate carbon fiber which is a semiconductor or a conductor. During the process, the fiber is broken and the processability is very poor and the carbon fiber cannot be obtained. The evaluation results are illustrated in Table 2.
Carbonization is performed in the same manner as in Comparative Example 3 except that the fiber to be heated is changed from the carbon fiber precursor to an intermediate carbon fiber which is a semiconductor or a conductor. During the process, the single filament is found severed and a large amount of fluff is generated. The evaluation results are illustrated in Table 2.
A carbon fiber is obtained by carbonizing in the same manner as in Example 7 except that the fiber to be heated is changed from the carbon fiber precursor to an intermediate carbon fiber which is a semiconductor or a conductor. The carbon content of the obtained carbon fiber is 90% by mass, no breakage of the fiber is found, and the processability is extremely good. The evaluation results are illustrated in Table 2.
A carbon fiber is obtained by heating in the same manner as in Example 8 except that the fiber to be heated is changed from the carbon fiber precursor to an intermediate carbon fiber which is a semiconductor or a conductor. Some single filaments are found broken during the process, and the heating subject fiber tends to wind around the conveying roll. The evaluation results are illustrated in Table 2.
A carbon fiber is obtained by heating in the same manner as in Example 9 except that the fiber to be heated is changed from the carbon fiber precursor to an intermediate carbon fiber which is a semiconductor or a conductor. Although some single filaments are found broken during the process, the processability is good. The evaluation results are illustrated in Table 2.
Carbonization is performed in the same manner as in Comparative Example 4 except that the fiber to be heated is changed from the carbon fiber precursor to an intermediate carbon fiber which is a semiconductor or a conductor. During the process, a large amount of fluff is generated on the fiber, and the fiber tends to be wound around the conveying roll. The carbon content of the obtained carbon fiber is 90%. The evaluation results are illustrated in Table 2.
Number | Date | Country | Kind |
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2021-015373 | Feb 2021 | JP | national |
Filing Document | Filing Date | Country | Kind |
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PCT/JP2022/003831 | 2/1/2022 | WO |