JP2018016921A - Method for manufacturing carbon fiber - Google Patents

Abstract

PROBLEM TO BE SOLVED: To provide a carbon fiber manufacturing method capable of manufacturing carbon fiber at relatively low cost.SOLUTION: A carbon fiber manufacturing method of the present invention includes the following steps of: obtaining ashless coal by solvent extraction treatment of coal; hydrogenating the ashless coal; performing heat treatment of the hydrogenated ashless coal; and melt spinning the heat-treated ashless coal. The molar ratio of the hydrogen content to the carbon content of the ashless coal (H/C) before the hydrogenation is 0.91 or less. The hydrogenation step includes the steps of: mixing the ashless coal with a hydrogen donor solvent; and heating the mixture obtained by the mixing, wherein the heating is preferably performed at 350°C or more and 500°C or less. The solvent extraction treatment is preferably performed at 300°C or more and 450°C or less. The heat treatment is preferably performed at 150°C or more and 350°C or less.SELECTED DRAWING: Figure 1

Description

  The present invention relates to a method for producing carbon fiber.

  Carbon fiber is widely used as a reinforcing material for structural materials such as resin, concrete, and ceramic. In addition, carbon fiber is also used as, for example, a heat insulating material, activated carbon raw material, conductive material, heat transfer material, and the like.

  The carbon fiber is generally produced by forming a synthetic resin such as polyacrylonitrile or a pitch obtained from petroleum or coal into a fiber shape by spinning, and making the yarn infusible (air oxidation) and carbonized. Among the above raw materials, coal pitch is a residue after removing volatile components such as naphthalene by distillation from coal tar, which is a liquid material by-produced when carbon is produced by carbonization to produce coke. Black material. Such a coal pitch is a mixture of many compounds containing many aromatic compounds containing many benzene rings in their skeletons.

  A method of melt spinning a coal extract has also been devised. In this method, the inventors have proposed a method for producing carbon fiber that uses inexpensive coal as a raw material, and performs spinning from ashless coal, which is an extract from coal, to remove insoluble components and then spins. (See Japanese Patent Application No. 2015-53477).

  However, in the above production method, since the yield of carbon fiber is reduced due to the removal of a part of the components of ashless coal in the second extraction step, an increase in the production cost of carbon fiber is avoided. I can't.

Japanese Patent Application No. 2015-53477

  In view of the above inconveniences, an object of the present invention is to provide a carbon fiber production method capable of producing carbon fiber at a relatively low cost.

  The invention made in order to solve the above-mentioned problems includes a step of obtaining ashless coal by solvent extraction treatment of coal, a step of hydrogenating the ashless coal, a step of heat treating the hydrogenated ashless coal, A step of melt spinning the heat-treated ashless coal, and producing a carbon fiber having a hydrogen content molar ratio (H / C) of 0.91 or less to the carbon content of the ashless coal before hydrogenation Is the method.

  In the carbon fiber production method, the ashless coal is hydrogenated to convert the high molecular weight component, which is a spinning inhibition component in the ashless coal, into a low molecular weight component, so that melt spinning is performed while suppressing a decrease in yield. A pitch for spinning (ashless coal) suitable for the above can be obtained. Moreover, the manufacturing method of the said carbon fiber uses the ashless coal whose molar ratio (H / C) of hydrogen content with respect to carbon content is 0.91 or less, and the pitch for spinning after hydrogenation is excessive. It is possible to prevent the spinnability from being lowered by including a low molecular weight component. As a result, the carbon fiber production method can produce carbon fiber at a relatively low cost.

  The hydrogenation step may include a step of mixing ashless coal with a hydrogen donating solvent and a step of heating the mixture obtained by the mixing, and the heating may be performed at 350 ° C. or higher and 500 ° C. or lower. By passing through such a hydrogenation step, the high molecular weight component in the ashless coal can be more reliably converted to the low molecular weight component.

  The solvent extraction treatment may be performed at 300 ° C. or higher and 450 ° C. or lower. By setting the temperature of the solvent extraction treatment within the above range, the extraction cost of ashless coal can be reduced.

  The heat treatment is preferably performed at 150 ° C to 350 ° C. By setting the temperature of the heat treatment within the above range, the spinnability of the carbon fiber can be enhanced while reducing the cost.

  Here, “content” means the mass proportion of atoms on an anhydrous ashless base (daf). “Hydrogen content” means the content of hydrogen atoms including not only hydrogen molecules but also atoms bonded to other atoms, and specifically measured according to JIS-M8813 (2004). Means the value to be

  As described above, the carbon fiber production method of the present invention can produce carbon fiber at a relatively low cost.

It is a flowchart which shows the procedure of the manufacturing method of the carbon fiber of one Embodiment of this invention.

  Hereinafter, embodiments of the present invention will be described in detail with reference to the drawings as appropriate.

[Method for producing carbon fiber]
As shown in FIG. 1, the carbon fiber manufacturing method includes an ashless coal acquisition step S1 for obtaining ashless coal by a solvent extraction process of coal, a hydrogenation step S2 for hydrogenating the ashless coal, A heat treatment step S3 for heat-treating the ash coal and a melt spinning step S4 for melt-spinning the heat-treated ashless coal are provided. The carbon fiber production method preferably includes an infusibilization step S5 for infusifying the filament obtained by the melt spinning, and a carbonization step S6 for carbonizing the infusible filament.

<Ashless coal acquisition process>
In ashless coal acquisition process S1, the slurry which mixed raw material coal and a solvent is heated more than the thermal decomposition temperature of raw material coal, and the soluble component of the pyrolyzed raw material coal is extracted to a solvent. Furthermore, an ashless coal is obtained by isolate | separating the insoluble component in the thermal decomposition temperature of raw material coal from this slurry. The “ashless coal” is a modified coal obtained by reforming coal and has an ash content of 5% or less, preferably 3% or less, more preferably 1% or less. In addition, "ash content" means the value measured based on JIS-M8812 (2004).

  Examples of coal used as a raw material for ashless coal include anthracite coal, bituminous coal, subbituminous coal, lignite, and the like in order of increasing degree of coalification. Among them, bituminous coal or subbituminous coal having a moderate degree of coalification is preferable.

  As a minimum of molar ratio (O / C) of oxygen content to carbon content of raw material coal, 0.01 is preferred and 0.03 is more preferred. On the other hand, the upper limit of the molar ratio (O / C) is preferably 0.20, and more preferably 0.12. If the molar ratio (O / C) is smaller than the lower limit, the content of the high molecular weight component that is a spinning inhibiting component in the obtained ashless coal increases, and spinning may be difficult. On the other hand, when the molar ratio (O / C) exceeds the upper limit, the extractability of coal into the solvent is lowered, and the yield of ashless coal may be lowered. Moreover, since the ratio of the low molecular weight component and oxygen in ashless coal becomes high, excessive pyrolysis may occur in the heat treatment described later, which may reduce the yield of the spinning pitch. The “oxygen content” means the content of oxygen atoms including not only oxygen molecules but also atoms bonded to other atoms, and specifically measured according to JIS-M8813 (2004). Means the value to be

  The solvent is not particularly limited as long as it has a property of dissolving the raw material coal. For example, monocyclic aromatic compounds such as benzene, toluene and xylene, bicyclic rings such as naphthalene, methylnaphthalene, dimethylnaphthalene and trimethylnaphthalene. Aromatic compounds, tricyclic aromatic compounds such as anthracene, and the like can be used. The bicyclic aromatic compound includes naphthalene having an aliphatic chain and biphenyl having a long aliphatic chain.

  Among the above solvents, a bicyclic aromatic compound which is a coal derivative purified from a coal carbonization product is preferable. The bicyclic aromatic compound of the coal derivative is stable even in a heated state and has an excellent affinity with coal. Therefore, by using such a bicyclic aromatic compound as a solvent, the ratio of coal components extracted into the solvent can be increased, and the solvent can be easily recovered and reused by a method such as distillation. .

  As a minimum of heating temperature (solvent extraction processing temperature) of slurry, 300 ° C is preferred, 350 ° C is more preferred, and 370 ° C is still more preferred. On the other hand, the upper limit of the heating temperature of the slurry is preferably 450 ° C, more preferably 420 ° C. When the heating temperature of the slurry is less than the above lower limit, the bond between the molecules constituting the coal cannot be sufficiently weakened, and the ratio of the coal component extracted into the solvent to the coal (hereinafter also referred to as the extraction rate) becomes low. There is a risk of economy. On the contrary, when the heating temperature of the slurry exceeds the above upper limit, the pyrolysis reaction of coal becomes very active, and the recombination of the generated pyrolysis radical occurs, resulting in a decrease in the extraction rate of ashless coal, which is uneconomical. There is a risk of becoming.

  The heating time of the slurry (the time for maintaining the heating temperature) can be, for example, 30 minutes or more and 2 hours or less. The solvent extraction may be performed in the presence of an inert gas, for example, in a nitrogen atmosphere at a pressure of 0.1 MPa to 2 MPa.

  The slurry after the solvent extraction treatment is separated into a filtrate and a solid content concentrate by filtration, for example, and the solvent is separated from the filtrate by distillation or the like, so that insoluble components are separated from the slurry. At this time, solid ashless coal can be obtained by cooling the slurry during or after separation.

  The extraction rate from coal in the ashless coal acquisition step S1 (the yield of ashless coal) depends on the quality of coal as a raw material, but is, for example, 20% by mass or more and 60% by mass on the basis of coal and air dry. % Or less.

  The upper limit of the molar ratio (H / C) of the hydrogen content to the carbon content of the ashless coal before the hydrogenation step S2 obtained in the ashless coal acquisition step S1 is 0.91, preferably 0.89. 0.85 is more preferable. If the molar ratio (H / C) exceeds the above upper limit, the amount of alkyl groups in the ashless coal is large, that is, the amount of low molecular weight components increases, so the ashless coal is excessively lowered in molecular weight by the hydrogenation step S2. As a result, spinnability may be reduced. In addition, although the minimum of the said molar ratio (H / C) is not specifically limited, For example, it is 0.7.

<Hydrogenation process>
In the hydrogenation step S2, the ashless coal obtained in the ashless coal acquisition step S1 is hydrogenated. Here, hydrogenation means donating hydrogen to a compound constituting ashless coal. Specifically, hydrogen is bonded to a high molecular weight hydrocarbon, thereby substituting it with a low molecular weight hydrocarbon. .

  The method for hydrogenation is not particularly limited, and hydrogenation with a hydrogen donating solvent, hydrogenation with hydrogen gas, or the like can be used, but it is preferable to use a hydrogen donating solvent. Specifically, hydrogenation process S2 is good to have a mixing process which mixes ashless charcoal with a hydrogen donating solvent, and a heating process which heats a mixture obtained by this mixing.

(Mixing process)
In the mixing step, a hydrogen donating solvent is mixed with the ashless coal obtained in the ashless coal acquisition step S1. The hydrogen-donating solvent is not particularly limited as long as it is an organic compound that can donate hydrogen to ashless coal by heating. For example, tetralin, tetrahydroquinoline, tetrahydrofuran, or the like can be used.

  The ashless coal is preferably pulverized before mixing with the hydrogen donating solvent. The diameter of the ashless coal after pulverization is preferably 1 mm or less. In addition, "diameter is 1 mm or less" means that particles pass through a metal mesh screen having a mesh size of 1 mm as defined in JIS-Z8801-1 (2006).

  The lower limit of the mixing amount of the hydrogen donating solvent with respect to 100 parts by mass of ashless coal is preferably 200 parts by mass, and more preferably 300 parts by mass. On the other hand, the upper limit of the mixing amount of the hydrogen donating solvent is preferably 1000 parts by mass, and more preferably 700 parts by mass. If the mixing amount of the hydrogen donating solvent is smaller than the above lower limit, the ashless coal may be insufficiently hydrogenated. On the contrary, when the mixing amount of the hydrogen donating solvent exceeds the above upper limit, the production cost of the carbon fiber may increase.

(Heating process)
In the heating step, the ashless coal is hydrogenated by heating the mixture of the ashless coal and the hydrogen donating solvent obtained in the mixing step.

  As a minimum of heating temperature, 350 ° C is preferred, 380 ° C is more preferred, and 400 ° C is still more preferred. On the other hand, as an upper limit of heating temperature, 500 degreeC is preferable and 450 degreeC is more preferable.

  The heating time (the time for maintaining the heating temperature) can be, for example, 30 minutes or more and 2 hours or less. This heating may be performed in the presence of an inert gas, for example, in a nitrogen atmosphere at a pressure of 0.1 MPa or more and 2 MPa or less.

  After the mixture is heated, solid hydrogenated ashless coal can be obtained by separating the solvent from the mixture by distillation or the like.

<Heat treatment process>
In the heat treatment step S3, the ashless coal hydrogenated in the hydrogenation step S2 is heat-treated to volatilize volatile components, and components that are thermally decomposed at low temperatures are decomposed and removed in advance. Thus, by previously removing volatile components and decomposable components that may hinder melt spinning, melt spinning becomes easier and carbon fibers having excellent tensile strength can be produced relatively inexpensively.

  The heat treatment is preferably performed in a non-oxidizing gas atmosphere. Thus, by heating in a non-oxidizing gas atmosphere to prevent oxidative crosslinking, inconveniences such as an increase in softening temperature can be prevented. The non-oxidizing gas is not particularly limited as long as it can suppress the oxidation of ashless coal, but nitrogen gas is more preferable from the economical viewpoint.

  The heat treatment is preferably performed in a reduced pressure state. Thus, by heat-processing in a pressure-reduced state, the vapor | steam of a volatile component and the gas of a thermal decomposition product can be efficiently removed from ashless coal.

  As a minimum of heat treatment temperature in heat treatment process S3, 150 ° C is preferred, 170 ° C is more preferred, and 200 ° C is still more preferred. On the other hand, the upper limit of the heat treatment temperature is preferably 350 ° C., more preferably 320 ° C., and further preferably 300 ° C. When the heat treatment temperature is less than the lower limit, volatile components in the insoluble components cannot be sufficiently removed, and the spinnability of the ashless coal (spinning pitch) after the heat treatment becomes insufficient, and the spinning efficiency May decrease. Conversely, if the heat treatment temperature exceeds the upper limit, the energy cost may increase unnecessarily, the useful components may be thermally decomposed and the production efficiency of the carbon fiber may decrease, and the carbonization may proceed and spinning. May decrease.

  The heat treatment temperature in the heat treatment step S3 is more preferably higher than the spinning temperature in the melt spinning step described later. In this way, by making the heat treatment temperature higher than the spinning temperature, the components that can be thermally decomposed during melt spinning can be previously thermally decomposed and removed in the heat treatment step S3. Thereby, it can prevent that the pyrolyzate produced | generated at the time of spinning breaks a filament, and forms these defects in the carbon fiber finally obtained.

  As a minimum of heat processing time (time to hold | maintain at the said heat processing temperature) in heat processing process S3, 10 minutes are preferable and 15 minutes are more preferable. On the other hand, the upper limit of the heat treatment time is preferably 120 minutes, and more preferably 90 minutes. When the heat treatment time is less than the lower limit, the volatile component may not be sufficiently removed. Conversely, if the heat treatment time exceeds the upper limit, the processing cost may be unnecessarily increased.

  The lower limit of the softening temperature of the ashless coal (spinning pitch) after the heat treatment is preferably 150 ° C, and more preferably 170 ° C. On the other hand, as an upper limit of the softening temperature of the ashless coal after heat processing, 280 degreeC is preferable and 250 degreeC is more preferable. When the softening temperature of the ashless coal after the heat treatment is less than the lower limit, the infusibilization temperature cannot be increased, and the infusibilization treatment may become inefficient. Conversely, when the softening temperature of the ashless coal after the heat treatment exceeds the above upper limit, it is necessary to increase the melt spinning temperature, which may cause spinning to become unstable and increase the cost. The “softening temperature” is a value measured by a ring and ball method in accordance with ASTM-D36.

  The yield of the ashless coal after the heat treatment from coal is preferably, for example, 20% by mass or more and 50% by mass or less on the basis of coal and air dry.

<Melt spinning process>
In the melt spinning step S4, melt spinning is performed using a known spinning device using the ashless coal heat-treated in the heat treatment step S3 as a spinning pitch. That is, the molten ashless coal is formed into a thread shape by passing through a nozzle (cap), and the shape of the ashless coal is fixed to the thread shape by cooling.

  From the viewpoint of preventing the softening point from being lowered, it is preferable to perform melt spinning without mixing a solvent with solid spinning pitch (ashless coal).

  As the nozzle used for the melt spinning, a known nozzle may be used. For example, a nozzle having a diameter of 0.1 mm to 0.5 mm and a length of 0.2 mm to 1 mm can be used. The filamentous body obtained by melt spinning ashless coal is wound, for example, by a drum having a diameter of about 50 mm to 300 mm.

  As a minimum of melt spinning temperature, 180 ° C is preferred, 200 ° C is more preferred, and 220 ° C is still more preferred. On the other hand, the upper limit of the melt spinning temperature is preferably 350 ° C, more preferably 300 ° C, and even more preferably 280 ° C. If the melt spinning temperature is less than the above lower limit, the ashless coal may be insufficiently melted and stable spinning may not be possible. On the contrary, when the melt spinning temperature exceeds the above upper limit, the spun filaments may be disconnected due to thermal decomposition of the components of ashless coal.

  Although it does not specifically limit as a minimum of the linear velocity of melt spinning, 100 m / min is preferable and 150 m / min is more preferable. On the other hand, the upper limit of the melt spinning linear velocity is preferably 500 m / min, and more preferably 400 m / min. When the line speed of melt spinning is less than the lower limit, the production efficiency is low and the carbon fiber may be expensive. On the other hand, when the linear speed of melt spinning exceeds the above upper limit, the spinning becomes unstable, so that the production efficiency is lowered, and the carbon fiber may still be expensive.

  The lower limit of the average diameter of the filaments spun in melt spinning is preferably 5 μm, more preferably 7 μm. On the other hand, the upper limit of the average diameter of the filaments spun in melt spinning is preferably 20 μm and more preferably 15 μm. When the average diameter of the filamentous body is less than the lower limit, there is a possibility that spinning cannot be stably performed. On the other hand, when the average diameter of the filamentous body exceeds the above upper limit, the flexibility of the filamentous body may be insufficient.

<Infusibilization process>
In the infusibilization step S5, the filamentous body obtained in the melt spinning step S4 is heated in an atmosphere containing oxygen to crosslink the filamentous body and make it infusible. Generally, air is used as the atmosphere containing oxygen.

  The lower limit of the infusibilization treatment temperature is preferably 150 ° C, more preferably 200 ° C. On the other hand, the upper limit of the infusibilization treatment temperature is preferably 300 ° C, and more preferably 280 ° C. When the infusibilization treatment temperature is less than the lower limit, infusibilization may be insufficient, or the infusibilization treatment time may be increased, resulting in inefficiency. Conversely, when the infusibilization temperature exceeds the above upper limit, the filamentous body may be melted before oxygen crosslinking.

  The lower limit of the infusibilization time is preferably 10 minutes, and more preferably 20 minutes. On the other hand, the upper limit of the infusibilization time is preferably 120 minutes, more preferably 90 minutes. If the infusibilization time is less than the lower limit, infusibilization may be insufficient. Conversely, if the infusibilization treatment time exceeds the above upper limit, the production cost of the carbon fiber may increase.

<Carbonization process>
In carbonization process S6, by heating and carbonizing the filamentous material infusible in infusibilization process S5, the filamentous material is carbonized to obtain carbon fibers.

  Specifically, after the infusibilized filament is charged into an arbitrary heating device such as an electric furnace, the inside is replaced with a non-oxidizing gas, and then heated while blowing the non-oxidizing gas into the heating device. .

  The heating temperature in the carbonization step S6 may be appropriately set depending on the characteristics required for the carbon fiber, and is not particularly limited, but the lower limit of the heating temperature is preferably 700 ° C and more preferably 800 ° C. On the other hand, the upper limit of the heating temperature is preferably 3000 ° C and more preferably 2800 ° C. When the said heating temperature is less than the said minimum, there exists a possibility that carbonization may become inadequate. On the other hand, when the heating temperature exceeds the upper limit, the manufacturing cost may increase from the viewpoint of improving the heat resistance of the facility and fuel consumption.

  The heating time in the carbonization step S6 may be appropriately set depending on the characteristics required for the carbon fiber, and is not particularly limited, but the heating time is preferably 15 minutes or longer and 10 hours or shorter. If the heating time is less than the lower limit, carbonization may be insufficient. On the other hand, when the heating time exceeds the upper limit, the production efficiency of carbon fibers may be reduced.

  The non-oxidizing gas is not particularly limited as long as the oxidation of the carbon fiber can be suppressed, but nitrogen gas is preferable from the economical viewpoint.

<Advantages>
In the carbon fiber production method, the ashless coal is hydrogenated to convert the high molecular weight component, which is a spinning inhibition component in the ashless coal, into a low molecular weight component, so that melt spinning is performed while suppressing a decrease in yield. A pitch for spinning (ashless coal) suitable for the above can be obtained. Moreover, the manufacturing method of the said carbon fiber uses the ashless coal whose molar ratio (H / C) of hydrogen content with respect to carbon content is 0.91 or less, and the pitch for spinning after hydrogenation is excessive. It is possible to prevent the spinnability from being lowered by including a low molecular weight component. As a result, the carbon fiber production method can produce carbon fiber at a relatively low cost.

[Other Embodiments]
The method for producing the carbon fiber is not limited to the above embodiment.

  The method for producing the carbon fiber may include steps other than those described above as necessary. Specifically, within a range that does not adversely affect each step, there may be a step such as a step of pulverizing raw coal, a step of removing foreign matters, or the like between or before and after each step.

  The carbon fiber production method may include a step of removing the spinning inhibition component of ashless coal, which is a spinning pitch. However, as described above, the carbon fiber production method includes ashless coal spinning inhibition. Since the components can be reduced, it is preferable not to include a step of removing the spinning inhibiting component from the viewpoint of reducing the production cost.

  EXAMPLES Hereinafter, although this invention is explained in full detail based on an Example, this invention is not interpreted limitedly based on description of this Example.

<Manufacture of carbon fiber>
0.5 kg of raw material coals (A to D) having the properties shown in Table 1 were pulverized to a diameter of 1 mm or less, mixed with 2.0 kg of methylnaphthalene and charged in an autoclave to form a nitrogen atmosphere having an initial pressure of 0.2 MPa. Next, the temperature was raised to 380 ° C. at a heating rate of 10 ° C./min, held at 380 ° C. for 1 hour, and immediately separated into a filtrate and a residue by filtration. The obtained filtrate was distilled under the conditions of 5 mmHg and 180 ° C. to recover solids (ashless coal (A to D)). Table 2 shows the properties and yields of these ashless coals (coal basis, air-dry basis). The ashless coal A is obtained from the raw coal A, and the ashless coals B to D are obtained from the raw coals B to D, respectively. Moreover, content of each atom in Table 1 and Table 2 is an anhydrous ashless base (daf).

  100 g of the obtained ashless coal was pulverized to a diameter of 1 mm or less, and 500 g of tetrahydrofuran (THQ) was added to prepare a mixed solution. This mixed solution was charged into an autoclave to form a nitrogen atmosphere having an initial pressure of 0.2 MPa. Next, it heated up to the temperature shown in Table 3 with the temperature increase rate of 10 degree-C / min, and cooled after hold | maintaining at this temperature for 1 hour. The cooled mixed liquid was distilled under the conditions of 3 mmHg and 200 ° C. to recover the solid content (hydrogenated ashless coal). Subsequently, the hydrogenated ashless coal was heat-treated at 230 ° C. in a nitrogen atmosphere, and the spinning pitches of Examples 1 to 7 and Comparative Examples 2 and 3 were obtained.

  In addition, as Comparative Example 1, 2.0 kg of methylnaphthalene was further added to ashless coal B obtained using raw coal B in the same procedure as in Example 1 and the like, and stirred at an extraction temperature of 60 ° C. for 1 hour. Soluble components were extracted and separated into filtrate and residue by filtration. The obtained filtrate was distilled under conditions of 5 mmHg and 180 ° C. to recover the solid content. This solid content was heat-treated at 230 ° C. in a nitrogen atmosphere to obtain the spinning pitch of Comparative Example 1.

  The obtained spinning pitch was filled in a spinning machine having a nozzle having a diameter of 0.2 mm and a length of 0.4 mm, and melt spinning was performed at 250 ° C. while applying pressure with nitrogen. The filamentous body obtained at this time was wound up on a drum having a diameter of 100 mm rotating at 600 rpm. The wound filaments were infusibilized by heating in air at 250 ° C. for 1 hour, and then carbonized at 800 ° C. to produce the carbon fibers of Examples 1-7 and Comparative Examples 1-3. It was. In Comparative Examples 2 and 3, the yarn was broken during winding, and spinning could not be performed.

<Evaluation>
About the obtained carbon fiber, the tensile strength was measured based on JIS-L1013 (2010). The results are shown in Table 3. In Comparative Examples 2 and 3, since no carbon fiber was obtained, the tensile strength was not measured. In addition, Table 3 also shows the yield (coal basis, air-dry basis) of spinning pitch (ashless coal after hydrogenation and heat treatment).

  From Table 3, melt spinning a spinning pitch obtained by hydrogenating and heat-treating ashless coal A to C having a molar ratio of hydrogen content to carbon content before hydrogenation (H / C) of 0.91 or less. Thus, it can be seen that carbon fiber of a certain quality can be obtained with a relatively high yield without requiring a step of removing the spinning inhibiting component.

  Moreover, it turns out that the carbon fiber which is excellent in tensile strength can be manufactured with a high yield by using the ashless coal A and B and making the heating temperature of hydrogenation 400 degreeC or more.

  On the other hand, Comparative Example 1 in which two-stage extraction was performed instead of hydrogenation had a lower pitch yield than Examples 4 and 5 using the same raw material coal B.

  In Comparative Examples 2 and 3 using ashless coal D having a molar ratio (H / C) of more than 0.91, the pitch yield was low and spinning could not be performed. This is probably because the ashless coal D contains a lot of low molecular weight components, and the low molecular weight components are further increased by hydrogenation, so that the pitch viscosity becomes too low. Moreover, it is thought that the fall of the yield of Comparative Examples 2 and 3 is due to an increase in low molecular weight components that volatilize in the heat treatment.

  Since the carbon fiber production method of the present invention can produce carbon fiber at a relatively low cost, it can be suitably used for products using carbon fiber as a raw material.

S1 Ashless coal acquisition step S2 Hydrogenation step S3 Heat treatment step S4 Melt spinning step S5 Infusibilization step S6 Carbonization step

Claims (4)

Obtaining ashless coal by solvent extraction treatment of coal;
Hydrogenating the ashless coal;
Heat treating the hydrogenated ashless coal;
A step of melt spinning the heat-treated ashless coal,
The manufacturing method of the carbon fiber whose molar ratio (H / C) of hydrogen content with respect to carbon content of the ashless coal before the said hydrogenation is 0.91 or less. The hydrogenation step is
Mixing ashless coal with a hydrogen-donating solvent;
Heating the mixture obtained by this mixing, and
The manufacturing method of the carbon fiber of Claim 1 which performs the said heating at 350 to 500 degreeC.   The carbon fiber manufacturing method according to claim 1 or 2, wherein the solvent extraction treatment is performed at 300 ° C or higher and 450 ° C or lower.   The method for producing a carbon fiber according to claim 1, wherein the heat treatment is performed at 150 ° C. or higher and 350 ° C. or lower.

Images