JP5724647B2 - Polyacrylonitrile-based copolymer, method for producing the same, carbon fiber precursor fiber, and carbon fiber - Google Patents

Description

  The present invention relates to a polyacrylonitrile-based copolymer and a method for producing the same, and a carbon fiber precursor fiber and a carbon fiber comprising the same.

  Carbon fiber has higher specific strength and specific modulus than other fibers, so as a reinforcing fiber for composite materials, in addition to conventional sports and aerospace applications, automobiles, civil engineering / architecture, pressure vessels and Widely used in general industrial applications such as windmill blades, there is a strong demand for both higher performance and lower costs.

  Among the carbon fibers, the most widely used polyacrylonitrile (hereinafter abbreviated as PAN) carbon fiber is a spinning solution composed of a PAN polymer as a precursor, and wet spinning or dry spinning. Alternatively, carbon fiber precursor fibers (hereinafter sometimes abbreviated as precursor fibers) are obtained by dry and wet spinning, and then heated in an oxidizing atmosphere at a temperature of 200 to 400 ° C. to make flame resistant fibers. And is produced industrially by heating and carbonization in an inert atmosphere at a temperature of at least 1000 ° C.

  The improvement in the productivity of PAN-based carbon fibers has been performed from the viewpoints of spinning, flame resistance or carbonization of carbon fiber precursor fibers. Among them, since flame resistance is an exothermic reaction, in order to suppress the exothermic runaway, the reaction temperature is controlled for a long time or the single fiber fineness of the PAN-based carbon fiber precursor fiber is reduced to a specific value or less. It is necessary to limit to the fineness, and the current flameproofing process is not a sufficiently efficient process.

  As one means for solving such a problem, a method for controlling the flameproofing reaction rate by copolymerizing acrylonitrile with acrylic acid, itaconic acid, acrylamide or the like is known (see Non-Patent Document 1). ). However, when these copolymer composition ratios are increased, an increase in adhesion between single fibers is induced, and the quality and physical properties of carbon fibers are lowered.

  Further, dimethylaminoethyl (meth) acrylamide has been proposed as a monomer copolymerizable with acrylonitrile (see Patent Document 1). However, in this proposal, there is no detailed description of the effect of promoting the flame resistance reaction, and the amount of copolymerization is Is also a generally known value of 10% by weight or less.

“Polymer Processing”, 1993, Vol. 42, No. 12, p574

JP 59-130320 A

  Therefore, in view of the background of the above-described conventional technology, an object of the present invention is to simultaneously satisfy the excellent flame resistance reaction acceleration and the excellent carbon fiber properties, which were difficult with the conventional technology, and a method for producing the same. And providing a carbon fiber precursor fiber and carbon fiber using the same.

The present invention is to solve the above problems, and the polyacrylonitrile copolymer of the present invention is obtained by copolymerizing acrylonitrile with dimethylaminopropylacrylamide and / or dimethylaminopropylmethacrylamide. , and the and the a acrylonitrile from 98 to 99.95 mol%, dimethylaminopropyl acrylamide and / or dimethylaminopropylmethacrylamide comprises from 0.05 to 2 molar%, the heat generation starting temperature measured by differential scanning calorimetry T is 210 ° C. or lower.

  One embodiment of the method for producing the polyacrylonitrile copolymer of the present invention is a copolymerization of acrylonitrile with dimethylaminopropylacrylamide and / or dimethylaminopropylmethacrylamide. Another embodiment of the method for producing a polyacrylonitrile copolymer of the present invention is a reaction of a copolymer of acrylonitrile and an unsaturated carboxylic acid with dimethylaminopropylamine.

  According to the acrylonitrile-based polymer of the present invention, a polyacrylonitrile-based copolymer having a significantly low flameproofing reaction starting point can be obtained even if the copolymer composition ratio is less than that of conventional materials. By using this polyacrylonitrile-based copolymer as a carbon fiber precursor fiber, it is possible to reduce the temperature or increase the speed of the flameproofing process, and it is possible to efficiently produce high-quality carbon fibers at low cost. .

  Moreover, according to the manufacturing method of the polyacrylonitrile-type copolymer of this invention, it is possible to manufacture said polyacrylonitrile-type copolymer efficiently.

FIG. 1 is a diagram (graph) showing an example of an exothermic behavior of a polyacrylonitrile copolymer measured using a differential scanning calorimeter (DSC).

  The present inventors can improve the productivity in the flameproofing process while maintaining the carbon fiber properties at a high strength by selecting the compound copolymerized with acrylonitrile and controlling the copolymer composition ratio within a specific range. And reached the present invention.

  The polyacrylonitrile copolymer in the present invention (hereinafter sometimes simply referred to as a PAN copolymer) is obtained by copolymerizing acrylonitrile and dimethylaminopropylacrylamide and / or dimethylaminopropylmethacrylamide. It is a polyacrylonitrile polymer.

  In the present invention, by using dimethylaminopropyl acrylamide and / or dimethylaminopropyl methacrylamide as a copolymerization component of acrylonitrile, the flameproofing reaction can be started at a lower temperature than conventional, and as a result, the flameproofing reaction. Can be completed in a short time, and productivity can be improved. Moreover, the amount of copolymerization components that can be completed in the same flameproofing time as before can be reduced, high heat resistance can be imparted, and adhesion between single yarns in the flameproofing process can be suppressed. The copolymerization amount of dimethylaminopropyl acrylamide and / or dimethylaminopropyl methacrylamide is 0.05 to 2.5 mol% with respect to 95 to 99.95 mol% of acrylonitrile. If the amount of the copolymerization component is less than 0.05 mol%, the progress of the flameproofing reaction is delayed, and the effects of the present invention may not be obtained. On the other hand, when the amount of the copolymer component exceeds 2.5 mol%, the heat resistance of the polymer becomes insufficient, and the carbon fiber physical property deterioration due to adhesion between single yarns may become remarkable. The amount of copolymerization component is more preferably 0.07 to 1.5 mol%, still more preferably 0.1 to 0.5 mol%.

  In addition, the PAN copolymer of the present invention can use two or more kinds of copolymer components, and is copolymerized by adding a vinyl compound copolymerizable with acrylonitrile other than dimethylaminopropylacrylamide and dimethylaminopropylmethacrylamide. It is also possible to do. Monomers that can be copolymerized include, for example, acrylic acid, methacrylic acid, itaconic acid and their alkali metal salts, ammonium salts and lower alkyl esters, acrylamide and its derivatives, allyl sulfonic acid, methallyl sulfonic acid and their Salts or alkyl esters can be used.

  In the present invention, as described above, the amount of dimethylaminopropyl acrylamide and / or dimethylaminopropyl methacrylamide as a copolymer component is 0.05 to 2.5 mol% with respect to 95 to 99.95 mol% of acrylonitrile. However, when the monomer amount is insufficient, the above-mentioned other copolymerization component (monomer) can be added and copolymerized as necessary.

  The weight average molecular weight (Mw) of the PAN-based copolymer in the present invention is preferably 10 to 1,000,000, more preferably 200 to 650,000, and further preferably 300 to 500,000. Further, the dispersity of the PAN-based copolymer of the present invention is represented by the ratio Mw / Mn of the weight average molecular weight (Mw) and the number average molecular weight (Mn), preferably 1.5 to 10, more preferably 1 .8-6, more preferably 2-4.

  In the present invention, various average molecular weights are measured by gel permeation chromatography and are obtained as polystyrene equivalent values. When the weight average molecular weight (Mw) exceeds 1,000,000, gelation tends to occur and stable spinning may be difficult. On the other hand, when the weight average molecular weight (Mw) is less than 100,000, there is a problem that yarn breakage is likely to occur in the yarn making process. If Mw / Mn also exceeds 10, a low molecular weight component is likely contained, so that yarn breakage during firing tends to occur.

  In the present invention, the heat generation start temperature is a rate of temperature increase of 10 ° C./min in an air atmosphere using a differential scanning calorimeter (hereinafter sometimes simply referred to as DSC) as shown in FIG. It is obtained from the measured exothermic curve and is defined as the temperature at the rising point of the exothermic peak appearing in the vicinity of 200 to 300 ° C. (the point at which 0.2 W / g exothermed from the baseline).

  Flame-resistant heat generation is heat generated when PAN undergoes a thermal oxidation reaction in an oxidizing gas and changes to a flame-resistant structure. If the amount of heat generated exceeds the amount of heat removed, the reaction cannot be controlled and thread breakage may occur.

  If the heat generation start temperature is lowered, the difference from the thermal decomposition temperature of PAN is increased, and an allowance for heat removal is obtained, which is very advantageous from the viewpoint of disaster prevention. Moreover, if the flameproofing treatment can be performed at a low temperature, the amount of heat released from the flameproofing furnace can be reduced, which is advantageous from the viewpoint of thermal efficiency.

  When the heat generation start temperature exceeds 210 ° C., the heat removal margin is insufficient for improving the efficiency of the flameproofing process. In addition, when the heat generation starting temperature is lower than 170 ° C., a flameproofing reaction may occur during polymerization and during storage of the polymer, which may cause problems in terms of storage stability and disaster prevention. Therefore, the heat generation start temperature is preferably 170 to 210 ° C, more preferably 175 to 205 ° C.

  Next, the manufacturing method of the polyacrylonitrile-type copolymer of this invention is demonstrated.

  One embodiment of the method for producing the polyacrylonitrile copolymer of the present invention is a copolymerization of acrylonitrile with dimethylaminopropylacrylamide and / or dimethylaminopropylmethacrylamide.

  In the present invention, the polymerization method for producing the PAN-based copolymer can be selected from a solution polymerization method, a suspension polymerization method, an emulsion polymerization method, etc., and acrylonitrile and a copolymer component are uniformly polymerized. For the purpose, it is preferable to use a solution polymerization method. In the case of polymerizing using the solution polymerization method, as the solvent, for example, a solvent in which PAN is soluble, such as an aqueous zinc chloride solution, dimethyl sulfoxide, dimethylformamide, and dimethylacetamide, is preferably used. Among these, dimethyl sulfoxide is preferably used from the viewpoint of the solubility of the PAN-based copolymer.

  Another embodiment of the method for producing a polyacrylonitrile copolymer of the present invention is a reaction of a copolymer of acrylonitrile and an unsaturated carboxylic acid with dimethylaminopropylamine.

  In this production method, first, a copolymer of acrylonitrile and an unsaturated carboxylic acid is prepared. Such a copolymer is known as an acrylonitrile copolymer suitable for a carbon fiber precursor fiber, and is disclosed together with its production method in many documents such as JP-A No. 2002-145960.

  Next, the above-mentioned copolymer of acrylonitrile and unsaturated carboxylic acid is reacted with dimethylaminopropylamine. That is, the carboxyl group in the copolymer derived from the unsaturated carboxylic acid is reacted with the primary amino group of dimethylaminopropylamine to be amidated.

  For example, the reaction of a copolymer using acrylic acid as an unsaturated carboxylic acid and dimethylaminopropylamine is represented by the following formula.

  Similarly, the reaction of a copolymer using methacrylic acid as an unsaturated carboxylic acid and dimethylaminopropylamine is represented by the following formula.

  In the reaction formulas (1) and (2) above, the formula in which all the carboxyl groups of the copolymer are reacted with dimethylaminopropylamine is shown. However, the reaction may be performed so as to leave a part of the carboxyl groups. .

  As the unsaturated carboxylic acid, acrylic acid and methacrylic acid described above are most preferable. It is also possible to use acrylic acid and methacrylic acid together. As other unsaturated carboxylic acids, itaconic acid, crotonic acid, maleic acid, fumaric acid and the like can be used.

  A preferred embodiment of the reaction between a copolymer of acrylonitrile and an unsaturated carboxylic acid and dimethylaminopropylamine will be described.

  The ratio of acrylonitrile and unsaturated carboxylic acid in the copolymer of acrylonitrile and unsaturated carboxylic acid is preferably 95 to 99.95 mol% for acrylonitrile and 0.05 to 5 mol% for unsaturated carboxylic acid. When the amount of unsaturated carboxylic acid is less than 0.05 mol%, the flameproofing reaction is slow and flameproofing at low temperatures may not proceed easily. On the other hand, if it exceeds 5 mol%, the heat resistance of the polymer becomes insufficient, and the physical properties of the carbon fiber may be deteriorated due to adhesion between single yarns. The amount of the copolymer component is more preferably 0.07 to 3.0 mol%, further preferably 0.1 to 2.0 mol%, and most preferably 0.1 to 1 mol%.

  Moreover, as a copolymer of acrylonitrile and unsaturated carboxylic acid, what copolymerized the vinyl compound copolymerizable with acrylonitrile other than unsaturated carboxylic acid can also be used. Examples of the copolymerizable vinyl compound include unsaturated carboxylic acid metal salts, ammonium salts and alkyl esters, acrylamide and derivatives thereof, allyl sulfonic acid, methallyl sulfonic acid and salts thereof, or alkyl esters. be able to.

  In the reaction of the copolymer of acrylonitrile and unsaturated carboxylic acid with dimethylaminopropylamine, the mass ratio of the two is 0.5 mol of dimethylaminopropylamine with respect to 1 mol of carboxyl groups present in the copolymer. It is preferable to be ˜5 mol. From the viewpoint of promptly proceeding the reaction, the amount is more preferably 0.8 to 4 mol, and further preferably 1.0 to 3.0 mol. When dimethylaminopropylamine exceeds 5 mol, the reaction proceeds rapidly, but dimethylaminopropylamine remaining after the reaction may lower the spinnability. On the other hand, when the amount is less than 0.8 mol, the reaction may not proceed promptly, or the carbon fiber precursor fiber obtained by spinning the copolymer may not proceed easily at low temperatures.

  The reaction of the copolymer of acrylonitrile and unsaturated carboxylic acid with dimethylaminopropylamine is preferably carried out in solution. As the solvent, dimethylformamide, dimethylacetamide, and dimethylsulfoxide, which are common solvents for both, are preferable.

  The reaction temperature of the copolymer of acrylonitrile and unsaturated carboxylic acid and dimethylaminopropylamine is preferably 100 to 220 ° C. More preferably, it is 130-220 degreeC, More preferably, it is 140-180 degreeC. When temperature is lower than 100 degreeC, reaction rate may be slow and reaction time may take too much. When the temperature exceeds 220 ° C., the temperature is considerably higher than the boiling point of dimethylaminopropylamine, so that dimethylaminopropylamine is distilled out of the system and the reaction may hardly proceed.

  Next, the manufacturing method of the carbon fiber of this invention is demonstrated.

  First, the above-mentioned PAN copolymer is dissolved in a solvent in which a PAN copolymer such as dimethyl sulfoxide, dimethylformamide, and dimethylacetamide is soluble to obtain a spinning solution. In the case of using solution polymerization, if the solvent used for the polymerization and the spinning solvent are the same, the step of separating the obtained polyacrylonitrile copolymer and re-dissolving in the spinning solvent becomes unnecessary.

  The copolymer concentration of the PAN-based copolymer solution can be arbitrarily adjusted depending on the amount of solvent used in the spinning solution, but is preferably in the range of 10 to 30% by mass. If the copolymer concentration is less than 10% by mass, the amount of solvent used is increased, which is not economical, and the coagulation rate in the coagulation bath is lowered, resulting in voids inside, and a dense structure may not be obtained. On the other hand, when the copolymer concentration exceeds 30% by mass, the viscosity increases and spinning tends to be difficult. Moreover, since the copolymer solution is easily gelled, it may not be stored for a long time. The copolymer concentration is more preferably 14 to 25% by mass, and most preferably 18 to 23% by mass.

  In the present invention, the copolymer concentration is the mass% of the PAN copolymer contained in the PAN copolymer solution. Specifically, after weighing the PAN-based copolymer solution, the PAN-based copolymer is dissolved in a solvent that does not dissolve the PAN-based copolymer and is compatible with the solvent used in the PAN-based polymer solution. After desolvation of the combined solution, the PAN copolymer is weighed. The copolymer concentration can be calculated by dividing the mass of the PAN copolymer after desolvation by the mass of the PAN copolymer solution before desolvation.

  In the present invention, the acrylic copolymer of the present invention is converted into a carbon fiber precursor fiber through steps such as spinning, washing with water, stretching in a bath, application of an oil agent, and drying according to a known method. The spinning may be performed directly in a coagulation bath, or may be coagulated in the bath after being once spun in air.

  The spun fiber is usually stretched in the bath at a stretching temperature of 30 to 98 ° C. by about 2 to 6 times after the solvent is removed in the water washing step, but the present invention is not limited to this. The water washing process may be omitted, and after spinning, the film may be stretched in a bath and then washed with water.

  It is preferable to apply an oil agent from the meaning of preventing adhesion between single fibers after the stretching step in the bath. As the component of the oil agent, for example, an oil agent containing a modified silicone such as amino-modified silicone is preferable from the viewpoint of heat resistance. The drying step is performed by drying the yarn after stretching in a bath with a hot drum or the like, and the drying temperature, time, and the like can be appropriately selected.

Further, if necessary, the dried and densified yarn is also subjected to pressure steam drawing.
The obtained carbon fiber precursor is usually in the form of a continuous multifilament (bundle), and the number of filaments is preferably 1,000 to 3,000,000, more preferably 6,000 to 36,000. It is a book. The fineness of the single fiber is preferably 0.5 to 1.5 dtex.

  Next, the carbon fiber precursor fiber produced by the above-described method is subjected to flameproofing treatment in air at a temperature of 200 to 300 ° C., preferably while stretching at a stretch ratio of 0.8 to 2.5, In an inert atmosphere at a temperature of 300 to 800 ° C., preferably pre-carbonized while stretching at a stretching ratio of 0.9 to 1.5, and in an inert atmosphere at a maximum temperature of 1,000 to 2,000 ° C. The carbon fiber is produced by carbonization while preferably drawing at a draw ratio of 0.9 to 1.1. Nitrogen, argon, xenon, etc. can be illustrated as gas used for an inert atmosphere, and nitrogen is preferably used from an economical viewpoint.

(Examples 1-8, Comparative Examples 1-3 : Examples 2-4 and 6-8 are examples of the present invention, and Examples 1 and 5 are reference examples. )
A copolymer component composed of acrylonitrile and the copolymer composition shown in Table 1 (the rest is acrylonitrile) is radically polymerized using azobisisobutyronitrile as an initiator by a solution polymerization method using dimethyl sulfoxide as a solvent, and polyacrylonitrile is obtained. A system copolymer was obtained. DMAPAA shown in the copolymerization component column of Table 1 means dimethylaminopropyl acrylamide, and DMAPMA means dimethylaminopropyl methacrylamide.

  The obtained copolymer was freeze-pulverized in liquid nitrogen and then passed through a sieve having an aperture of 0.5 mm to obtain a powder. 5 mg of the obtained powder was accurately weighed, filled into an aluminum pan size (φ6.7 × 1.5H) manufactured by BRUKERaxs in an open system, and used in an air stream of 30 mL / min using a DSC3100SA manufactured by BRUKERaxs. DSC measurement from 30 ° C to 450 ° C at a heating rate of ℃ / min, corresponding to the rising point of the exothermic peak that appears around 200-300 ° C (the point where 0.2 W / g exothermed from the baseline) The temperature at which the heat generation was performed was read and used as the heat generation start point T (° C.). The baseline was the point at which the exothermic rate immediately before the exothermic peak was 0 W / g · s.

  Next, the concentration of the copolymer was adjusted to 20% by mass in dimethyl sulfoxide to prepare a spinning dope. The obtained spinning dope is passed through a filter having a mesh opening of 0.5 μm, and then discharged into the air at a temperature of 40 ° C. using a spinneret having a single hole diameter of 0.15 mm and a hole number of 500, and about 4 mm. After passing through the space, a coagulated yarn was obtained by a dry and wet spinning method introduced into a coagulation bath composed of an aqueous solution of 35% by mass dimethyl sulfoxide controlled at a temperature of 3 ° C. The coagulated yarn thus obtained was washed with water by a conventional method, then stretched 3.5 times in warm water at 60 ° C., and further provided with an amino-modified silicone silicone oil to give a single fiber fineness of 2.6 dtex. A drawn yarn was obtained in the bath. The drawn yarn in the bath is subjected to a drying heat treatment using a roller heated to a temperature of 165 ° C., then drawn 3.7 times in a pressurized steam at a temperature of 145 ° C., and the total draw ratio is 13 times. A carbon fiber precursor fiber having a fiber fineness of 0.7 dtex and a filament count of 500 was obtained.

  Six of the obtained carbon fiber precursor fibers were combined to make a total filament number of 3,000, and subjected to a flame resistance treatment while being drawn at a draw ratio of 1.0 in air at a temperature of 240 ° C. Subsequently, in a nitrogen atmosphere at a temperature of 300 to 700 ° C., a preliminary carbonization treatment is performed while stretching at a stretch ratio of 1.15, and in a nitrogen atmosphere at a maximum temperature of 1500 ° C., the stretch ratio is set to 0.99. Carbonization was performed to obtain carbon fibers having a specific gravity of 1.80 to 1.83.

At this time, on the exit side of the carbonization step, the number of fluffs of the running yarn is visually measured over a length of 30 m, and the number of fluffs per meter is defined as the number of fluffs (number / m). Evaluation was made in three stages.
Grade ○: Number of carbonized fluff 0-20 pieces / m
Grade △: Number of carbonized fluff 21 pieces / m or more Grade ×: Broken carbonized yarn.

  Moreover, about the obtained carbon fiber, the tensile strength and the tensile elasticity modulus were calculated | required according to JISR7601 (1986) "resin impregnation strand test method". Here, the resin-impregnated strand of carbon fiber to be measured was “BAKELITE” (registered trademark) ERL 4221 (100 parts by mass) / 3 boron trifluoride monoethylamine (3 parts by mass) / acetone (4 masses) manufactured by Union Carbide Corporation. Part) was impregnated into carbon fiber, and was hot-treated at 130 ° C. for 30 minutes and cured. The number of strands measured was 6, and the arithmetic average value of each measurement result was taken as the tensile strength and tensile modulus of the carbon fiber. The results are shown in Table 1.

DMAPAA: dimethylaminopropyl acrylamide DMAPMA: dimethylaminopropyl methacrylamide (Examples 9 to 15 and Comparative Example 4) Examples 9 to 14 are examples of the present invention, and Example 15 is a reference example. )
Radical polymerization of acrylonitrile and acrylic acid with the composition shown in Table 2 (the rest is acrylonitrile) using azobisisobutyronitrile as an initiator by solution polymerization using dimethyl sulfoxide as a solvent. A solution containing the polymer was obtained.

  After the obtained copolymer solution was transferred to a reaction vessel equipped with a reflux condenser and a stirrer, dimethylaminopropylamine was added in an amount of 1. to 1 mol of the carboxyl group of the copolymer as shown in Table 2. After adding so that it might become 0-2.3 mol, it was made to amidate at 180 degreeC, flowing nitrogen, for 5 hours, and the polyacrylonitrile-type copolymer was obtained.

  The heat generation start temperature was measured as in Examples 1-8. Similarly, carbon fiber precursor fibers are prepared, flame resistant, and carbonized to evaluate carbonization processability. The tensile strength and tensile elastic modulus of the obtained carbon fiber were measured.

As shown in Table 2, in Examples 9 to 14 , the heat generation start temperature of the copolymer is low, and the obtained carbon fiber precursor fibers are excellent in carbonization processability. Also, carbon fibers having high tensile strength and tensile modulus were obtained.

(Examples 16 to 20, Comparative Example 5 : Examples 16 to 19 are examples of the present invention, and Example 20 is a reference example. )
Using acrylonitrile and methacrylic acid in the composition shown in Table 2 (the rest is acrylonitrile), radical polymerization was carried out using azobisisobutyronitrile as an initiator by a solution polymerization method using dimethyl sulfoxide as a solvent. A solution containing the polymer was obtained.

  After the obtained copolymer solution was transferred to a reaction vessel equipped with a reflux condenser and a stirrer, 1 mol of dimethylaminopropylamine was added to 1 mol of carboxyl groups of the copolymer as shown in Table 2. Then, an amidation reaction was performed at 180 ° C. for 5 hours while flowing nitrogen to obtain a polyacrylonitrile-based copolymer.

  The heat generation start temperature was measured as in Examples 1-8. Similarly, carbon fiber precursor fibers are prepared, flame resistant, and carbonized to evaluate carbonization processability. The tensile strength and tensile elastic modulus of the obtained carbon fiber were measured.

As shown in Table 2, in Examples 16 to 19 , the heat generation start temperature of the copolymer is low, and the obtained carbon fiber precursor fibers are excellent in carbonization processability. Also, carbon fibers having high tensile strength and tensile modulus were obtained.

  In the present invention, by using a PAN-based polymer having a low flame-resistant reaction start temperature as a carbon fiber precursor fiber, it becomes possible to perform low-temperature or high-speed treatment in the flame-proofing process, and carbon fiber having good quality even in the subsequent carbonization process. Can be produced and is useful.

Claims (5)

Acrylonitrile and a 98 to 99.95 mol%, a copolymer containing a dimethylaminopropyl acrylamide and / or dimethylaminopropylmethacrylamide 0.05 to 2 molar%, the heat generation starting measured by differential scanning calorimetry A polyacrylonitrile copolymer having a temperature T of 210 ° C. or lower. A method for producing a polyacrylonitrile copolymer according to claim 1, characterized in that acrylonitrile is copolymerized with dimethylaminopropylacrylamide and / or dimethylaminopropylmethacrylamide. Manufacturing method of coalescence. A method for producing a polyacrylonitrile-based copolymer according to claim 1, characterized in that a copolymer of acrylonitrile and an unsaturated carboxylic acid is reacted with dimethylaminopropylamine. A method for producing a polymer. Polyacrylonitrile copolymer according to claim 1, or a polyacrylonitrile copolymer obtained by the method according to claim 2 or 3, carbon fiber precursor fiber obtained by spinning. Carbon fiber obtained by making the carbon fiber precursor fiber according to claim 4 flame resistant and carbonized.

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