JPH05171511A - Production of acrylic yarn - Google Patents

Abstract

PURPOSE:To produce an acrylic yarn not causing the mutual adhesion of single filaments and useful for carbon fibers, etc., superior in productivity of its production facility by subjecting a specific yarn to a drawing treatment in a hot water bath and subsequently nipping the drawn yarn at a yarn temperature of <=a prescribed value to remove the aqueous solution. CONSTITUTION:A yarn 1 is drawn in a hot water bath 2 and subsequently nipped with nip rollers 8 to remove or squeeze the bath solution. In the process, the temperature of the yarn 1 before fed into the nip rollers 8 is controlled at <=70 deg.C for the production of the acrylic yarn. The yarn 1 comprises an acrylic polymer mainly constituted of acylonitrile, has a yarn density index M of >=2000, the index M being represented by an equation: M=(the substantial total deniers [d] per yarn fed into the drawing in the bath)/(the width [mm] of the yarn per yarn), and has a single filament number of >=3000 per yarn.

Description

Detailed Description of the Invention

[0001]

BACKGROUND OF THE INVENTION The present invention can be applied to a method for producing acrylic yarns, more specifically for thick yarns and high-density filament yarns, and particularly for adhesion between single yarns in a dry densification step. The present invention relates to a method for producing an acrylic yarn that rarely occurs.

[0002]

2. Description of the Related Art Heretofore, in order to obtain carbon fibers having excellent performance, many improvements have been disclosed for polyacrylonitrile fiber which is a raw yarn (precursor). Carbon fiber is a spinning process of spinning a polyacrylonitrile-based fiber which is a precursor thereof, a flame-proofing process of heating the fiber in an air atmosphere of 200 to 400 ° C. to convert it into an oxidized fiber, nitrogen, helium, argon, etc. Obtained by going through a carbonization process (heating treatment process and carbonization process are collectively called a firing process) of further heating and carbonizing at 300 to 2500 ° C. in an inert atmosphere of aerospace. Widely used for applications, sports, general industrial applications, etc.

Among these uses of carbon fiber, it is most important to reduce the manufacturing cost and provide a low-priced carbon fiber in order to meet the demand for expanding the use to general industrial fields. To reduce the manufacturing cost, the yarn to be treated is thickened (thickened) in order to improve the equipment productivity, that is, to increase the production amount per unit equipment, and the yarn to be treated is occupied by the device. If the width to be narrowed (increased in density) occurs, the following problems occur.

When the yarn unit is thickened or densified, the solution permeability into the yarn becomes poor in the drawing process in the bath during the yarn making process, and the individual filaments are heated when the temperature rises. Is difficult to reach. Therefore, problems such as occurrence of adhesion between single yarns, deterioration of drawability, fluff, yarn breakage, or insufficient washing with water occur, and process passability decreases. Further, in the dry densification step after the drawing step in the bath or in the firing step, yarn breakage and fluffing also occur, the process passability is lowered, and the physical properties of the obtained carbon fiber are also lowered. As a means for stably performing hot water drawing in a drawing step in a bath, a multistage drawing method has been proposed in Japanese Patent Application Laid-Open No. 50-154531. However, even if it is adopted for the drawing of thick yarns and high-density yarns, the solution permeability into the yarns is poor, the occurrence of adhesion between single yarns cannot be suppressed, and the process passability is reduced. The fiber physical properties were also not sufficient.

Further, JP-A-64-68559, JP-A-64-85305 and JP-A-64-853.
No. 06 publication, in the yarn washing process, the oil agent applying process, and the hot water drawing process, the washing water, the oil agent, and the bath liquid are jetted from the yarn direction change guide, whereby the washing efficiency and the uniformity of the oil agent application are obtained. It is proposed to improve adhesion and prevent single yarn-to-yarn adhesion. However, when processing thick yarns or high-density yarns, the tension of the yarns applied to the direction change guide becomes particularly large, and the single yarns inside the yarn bundle are mutually constrained. It was difficult to prevent the oil agent from penetrating into the inside of the yarn, and the adhesion between single yarns could not be prevented. Further, in the dry densification step performed before the firing step, there is a problem that the adhesion between single yarns becomes more remarkable.

[0006]

DISCLOSURE OF THE INVENTION An object of the present invention is to provide a spinning method capable of solving the above-mentioned problems that occur when spinning thick yarns and high-density acrylic yarns, and more specifically a bath. After the medium stretching process, in the process of removing or squeezing the bath liquid from the yarn to be treated using a nip roller, it is possible to suppress the occurrence of adhesion between single yarns and evenly apply the process oil agent, which is a good process. An object of the present invention is to provide a method for producing an acrylic yarn, which has a passability and is capable of obtaining a high-quality precursor.

[0007]

The above-mentioned object of the present invention has a yarn density index M shown below of 200, which is mainly composed of an acrylic polymer mainly containing acrylonitrile as a constituent.
In the process of removing or squeezing the bath liquid by drawing a yarn having 0 or more and 3000 or more single yarns constituting the yarn in a hot water bath, and sandwiching the yarn with a nip roller, A method for producing an acrylic yarn, characterized in that the temperature of the yarn before entering the nip roller is 70 ° C. or lower, M = (substantially total denier per yarn used for drawing in the bath [d ] / (Yarn width per yarn [mm]).

The present invention will be described in detail below. The acrylic polymer used in the present invention is a polymer mainly composed of acrylonitrile, specifically, a polymer composed of 90% by weight or more of acrylonitrile, and is copolymerized with another comonomer within 10% by weight. May be. As comonomers, acrylic acid, methacrylic acid, itaconic acid, and the like, and their alkyl esters such as methyl ester, ethyl ester, propyl ester, butyl ester, alkali metal salts, ammonium salts, or allyl sulfonic acid, methallyl sulfonic acid, Examples thereof include styrene sulfonic acid and the like and alkali metal salts thereof, but are not particularly limited. When the amount of the comonomer exceeds 10% by weight, the physical properties of the finally obtained carbon fiber deteriorate, which is not preferable. The acrylic polymer is polymerized by a usual polymerization method such as emulsion polymerization, bulk polymerization and solution polymerization.

The acrylic polymer, dimethylacetamide, dimethylsulfoxide, dimethylformamide,
An acrylic fiber can be obtained by spinning using a polymer solution composed of nitric acid, an aqueous solution of rhodanese, etc. as a spinning dope by a usual wet spinning method or a dry wet spinning method.

For the purpose of improving equipment productivity, the yarn density index M defined by the following formula is 2000 d / mm or more. More preferably, it is 3000 d / mm or more. M = (substantial total denier per yarn used for drawing in the bath [d]) / (yarn width per yarn [mm]) Here, “substantial total denier per yarn” means swelling with a solution. It is not a denier of the yarn in the state of being denier, but a denier as a yarn consisting only of an acrylic polymer, and is a number obtained by multiplying the denier of the single yarn forming the yarn by the number of the single yarns forming the yarn is there. Further, the yarn width per yarn means the yarn width occupied by the one yarn provided for drawing in the drawing process in the bath, and the yarn width occupied by one yarn on the feed roller during drawing in the bath. Required from.

When the yarn density index M is less than 2000, the adhesion between single yarns in the drawing step in the bath as described above is not so remarkable without using the present invention, but the equipment productivity is improved. It is not possible because it cannot be done. Further, in order to remarkably obtain the productivity improving effect of the present invention, the number of single yarns constituting the yarn is 3000 or more. It is preferably 4500 or more, more preferably 6000 or more.

The most characteristic feature of the present invention is that in the step of removing or squeezing the bath liquid from the yarn to be treated using a nip roller after the drawing treatment in a hot water bath, the temperature of the yarn to be treated is Is cooled to 70 ° C. or lower. Cooling to 60 ° C. or lower is more preferable. Hot water here is 7
Water with a temperature above 0 ° C.

The temperature of the yarn before entering the nip roller is 7
When the temperature exceeds 0 ° C, the yarns are pressed against the nipple roller to cause single-yarn adhesion, or the oil agent is not uniformly applied, which is not preferable. In the case of thick yarns and high-density yarns, the thus-generated single yarn-to-single yarn adhesion causes more remarkable single-to-yarn adhesion in the drying and densifying step after application of the process oil agent. The method of cooling the yarn before entering the nip roller is not particularly limited, but the yarn is cooled by, for example, dipping in a cold water bath or spraying cold water to reduce the temperature of the yarn to 70
It can be kept at or below ° C.

The method of the present invention will now be described in more detail with reference to the drawings. FIG. 1 is a schematic sectional view showing an example of the method of the present invention. The yarn 1 is stretched in the stretching bath 2 using hot water exceeding 70 ° C. due to the difference in peripheral speed between the supply roller 6 and the take-up roller 7. The drawn yarn is sprayed with cold water by the cold water shower device 4 and also cooled in the cooling water receiving tank 3 to 70 ° C.
It becomes the following. The cooled yarn is nipped by the nip roller 8 to remove or squeeze the bath liquid, and is introduced into the process oil bath 5 to apply the process oil.

In the drawing step in the bath of the present invention, it is preferable to reduce the number of rollers involved, because it is possible to avoid the adhesion between single yarns which can be caused by the pressure applied to the drawing roller due to the drawing tension. In addition, when processing with multiple baths, it is possible to make the stretching tension more uniform by using a non-driving method (free rotation method) for the rollers between the baths than a general driving method. It is preferable because the effect of the present invention can be more remarkably obtained. Further, it is also effective to vibrate the yarn to be treated at a frequency of about 5 to 100 Hz, and it is preferable to combine these methods so that the adhesion between single yarns can be more effectively prevented.

Although the technical reason for the effect of suppressing the adhesion between single yarns in the present invention is not clear, by setting the yarn temperature to 70 ° C. or less before entering the nip roller, the acrylic yarn becomes glass transition. Since it is below the temperature, deformation and fusion of the yarns when passing through the nip roller are less likely to occur and adhesion between single yarns is suppressed, or the temperature of the oil agent bath rises due to the yarns to be treated in the next oil agent applying step. Becomes difficult,
It is considered that since the dispersed state of the oil agent is kept stable and the oil agent can be uniformly applied, the adhesion between single yarns is suppressed in the drying and densifying step.

[0017]

The present invention will be described in more detail with reference to the following examples. The characteristic values in the examples are obtained by the following method. (1) Yarn temperature The temperature of the running yarn was measured with a contact-type yarn thermometer. (2) Adhesion judgment of drawn yarn and dry densified yarn The drawn yarn or densified yarn is cut into about 5 mm and Neugen S is cut.
Disperse in 0.1% by weight aqueous solution of S, and stirrer 60
After stirring at rpm for 1 minute, filter with black filter paper to remove the adhesive state to 5
Visual evaluation was performed at each stage. 1 when no adhesion is observed
Grade, the state in which most of the single yarns are adhered was ranked as grade 5. In the case of grade 4 or higher, the adhesion level cannot be adopted from the viewpoints of the yarn-forming property and the physical properties of the carbon fiber after firing. (3) Stretchability of pressurized steam The number of single yarn breakages that occur in 10 minutes during pressurized steam stretching is measured by observing the running yarns, and 2 or less per minute is ◯, 6 or more per minute. Was designated as ×, and its middle was designated as Δ. (4)
Carbon fiber strength The strength of the epoxy resin-impregnated strand measured according to JIS R-7601 was measured 10 times, and the average value was obtained.

Examples 1 and 2, Comparative Examples 1 to 4 Dimethyl containing 20% by weight of an acrylonitrile copolymer having an intrinsic viscosity [η] of 1.80, which is composed of 99.5 mol% of acrylonitrile and 0.5 mol% of itaconic acid. A sulfoxide (hereinafter abbreviated as DMSO) solution was used as a spinning stock solution and spun from a spinneret of 12000H into a coagulation bath composed of DMSO and water to obtain coagulated yarns (total denier: 144000d) consisting of 12000. This coagulated yarn was washed with hot water, and then led to a drawing process in a bath consisting of 5 tanks, which was composed of free rollers except for the input roller of the first tank and the exit roller of the fifth tank, and the yarn width was 40 mm. While controlling, 5 times stretching was performed in hot water at 90 ° C. afterwards,
After the wet yarn was cooled in a cold water bath, it was nipped to squeeze the bath liquid and then led to an oil bath. In the cold water bath, the amount of water in the cold water bath was changed, and the temperature of the yarn before the nip was changed as shown in Table 1 to obtain yarns (Examples 1 and 2, Comparative Examples 1 and 2). Further, the wet yarn was nipped without cooling and the bath liquid was squeezed and then introduced into an oil bath to obtain a yarn (Comparative Example 3).

The application of the oil agent to the yarn is carried out by impregnating the amino modified silicone (the content of the amino group is 1.0% as NH ₂ ) into the bath solution of the oil agent which is emulsified with the nonylphenol EO adduct. And added 0.7% as oil.

After that, dry densification was carried out, and the measurement results of the adhesion between single yarns of the obtained densified yarn are also shown in Table 1. The single yarn-to-single yarn adhesion of the drawn yarn immediately after drawing in the bath was of the second grade. After the dry densification step, pressure steam drawing was performed (total magnification: 12 times) to obtain an acrylonitrile fiber yarn having a single fiber denier of 12,000 and a total fineness of 12,000 denier. The pressure steam stretchability at that time was evaluated and is also shown in Table 1. Further, the obtained yarn was subjected to flameproofing treatment in air at 200 to 280 ° C., then introduced into a carbonization furnace having a maximum temperature of 1300 ° C., and carbonized in a nitrogen atmosphere to obtain carbon fibers. The carbon fiber strength was measured and is also shown in Table 1. On the other hand, except that the yarn width is 120 mm and the yarn is not cooled before the nip, the dry densified yarn of the carbon fiber (Comparative Example 4) obtained by the same method as described above is bonded and bonded between single yarns. The pressure steam drawability and the carbon fiber strength are shown in Table 1.

[0021]

[Table 1] As can be seen in comparison with Comparative Examples 3 and 4, the yarns nipped at a yarn temperature within the range of the present invention (Examples 1 and 2) have a high yarn density, but a dry densified yarn. There was little adhesion between the single yarns, the pressure steam drawability was good, and a high-strength carbon fiber was obtained. On the other hand, in the case where the nip was performed at the yarn temperature which is outside the range of the present invention (Comparative Examples 1 to 3), adhesion between dry densified yarns between single yarns occurred, the pressure steam stretchability was lowered, and carbon The fiber strength was low. Moreover, when the yarn density index is less than 2000 (Comparative Example 4), the productivity improving effect is small, which is not preferable.

[0022]

According to the method of the present invention, after the thick yarn and the high-density yarn are drawn in the bath, the bath liquid can be removed without adhesion between single yarns and the process oil can be uniformly applied. The occurrence of adhesion between single yarns can be suppressed in the drying and densifying step.

By the method of the present invention, it becomes possible to uniformly and stably produce thick yarns and high-density filament yarns, and it is possible to dramatically improve equipment productivity. Therefore, it becomes possible to manufacture high-quality and high-performance carbon fiber at low cost, and its industrial effect is extremely large.

[Brief description of drawings]

FIG. 1 is a schematic sectional view showing an example of the method of the present invention.

[Explanation of symbols] 1: Thread 2: Drawing bath 3: Cooling water receiving tank 4: Cold water shower device 5: Process oil bath 6: Supply roller 7: Take-up roller 8, 8 ': Nip roller 9: Fixed roller

─────────────────────────────────────────────────── ─── Continuation of the front page (51) Int.Cl. ⁵ Identification code Internal reference number FI Technical display location D02J 1/22 301 B (72) Inventor Akira Okuda 1515 Tsutsui, Matsumae-cho, Iyo-gun, Ehime Toray Co., Ltd. Company Ehime Plant (72) Inventor Hideo Saruyama 1515 Tsutsui, Matsumae-cho, Iyo-gun, Ehime Prefecture Toray Co., Ltd. Ehime Plant

Claims (2)

[Claims] 1. A yarn density index M shown below consisting mainly of an acrylic polymer having acrylonitrile as a constituent component.
In the process of removing or squeezing the bath liquid by drawing a yarn having a number of 2000 or more and the number of single yarns constituting the yarn of 3000 or more in a hot water bath, and sandwiching the yarn with a nip roller. A method for producing an acrylic yarn, wherein the temperature of the yarn before entering the nip roller is 70 ° C. or lower. M = (substantial total denier [d] per yarn used for drawing in the bath) / (thread width [mm] per yarn) 2. The method for producing an acrylic yarn according to claim 1, wherein a step oil agent is applied after the step of removing or squeezing the bath liquid.