KR20050041350A - Uncoated airbag fabrics using low shrinkage trilobal polyamide fibers - Google Patents

Abstract

The present invention comprises the steps of (A) weaving a low shrinkage triangular cross-section polyamide fiber having a dry heat shrinkage of 3 to 6% with a dough for airbags, (B) three to three to increase the temperature sequentially by 5 to 20 ℃ Thermal shrinkage by continuously passing ten aqueous baths; (C) further thermal contraction by passing the fabric passed through the aqueous bath through a steam heater; and (D) passing the fabric through the steam heater through a hot air dryer. It relates to a fabric for an uncovered air bag produced by a method comprising the step of drying.

In addition, the prepared uncoated airbag fabric of the present invention has a high tensile strength and tear strength, good quality of the fabric can be usefully used as an uncoated fabric for airbags.

Description

Uncoated airbag fabrics using low shrinkage trilobal polyamide fibers}

The present invention comprises the steps of (A) weaving a low shrinkage triangular cross-section polyamide fiber having a dry heat shrinkage (190 ℃, 15 minutes) of 3 to 6% in the dough for air bags, (B) the dough by 5 to 20 ℃ sequentially Thermally contracting through three to ten aqueous baths having elevated temperature, (C) further heat shrinking the fabric passing through the aqueous bath by passing it through a steam heater, (D) passing through the steam heater The present invention relates to an uncoated airbag fabric manufactured by the method comprising the step of passing the fabric through a hot air dryer.

In addition, the prepared uncoated airbag fabric of the present invention has a high tensile strength and tear strength, good quality of the fabric can be usefully used as an uncoated fabric for airbags.

In recent years, airbags are indispensable as devices for securing the safety of passengers in vehicles, and the installation rate on vehicles has gradually increased.

The requirements for airbags include a variety of things, such as low breathability for smooth deployment in the event of a crash, high strength to prevent damage and rupture of the bag itself, and furthermore flexibility for preventing passenger face scratches during deployment. In recent years, the airbag fabric itself has become an important requirement in terms of the foldability of the fabric itself, the improvement of the storage properties, and the cost reduction.

Regarding the shape of the air bag, it is roughly divided into a so-called coat fabric in which resin is applied to the surface of the fabric after weaving and a non-coat fabric using the fabric after weaving. It is advantageous.

Until now, many techniques for realizing an airbag excellent in foldability and small in storage volume without impairing the strength and low breathability suitable as an airbag have been disclosed. For example, Japanese Patent Laid-Open No. 1-41438 discloses strength 8.5. It is said that the above object is achieved by using an airbag fabric composed of yarns composed of fibers having a g / d or more and single yarn fineness of 3 deniers or less. Although not mentioned at all, it is substantially related to a so-called coated fabric in which an elastomer such as chloroprene is coated on the surface of the fabric. When the technique is applied to an uncoated fabric, it is certainly satisfied with respect to strength and storage property. However, it was not satisfactory enough in terms of maintaining low breathability.

In addition, Japanese Unexamined Patent Application Publication No. 4-201650 discloses an air bag having excellent strength and foldability by using a polyamide multifilament made of a plurality of single yarns having a single cross section having a single yarn fineness of 1.0 to 12 deniers and a single yarn strain of 1.5 to 7.0. However, a technique for obtaining a woven fabric is disclosed. However, the technique also satisfies the required characteristics as an airbag woven fabric only when applied to a coat woven fabric. Was left.

As a technique related to an uncoated fabric, there is a method described in Japanese Patent Application Laid-Open No. 7-252740. In the publication, by using a flatness of 1.5 or more and a flat cross-section yarn, a fabric for an uncoated air bag which is excellent in low air permeability, foldability, and storage property can be obtained. However, in this technique, the air permeability under low pressure (124 Pa) is 0.3 cc / cm 2 / sec or more, and it is not possible to sufficiently satisfy the air permeability lower than that required in recent years.

On the other hand, in order to cope with the US regulation FMVSS208 as amended in 2000, dualization of inflator is considered. Since this inflator is a two-stage deployment system, the gas output of the second stage is higher than that of the conventional inflator. Therefore, it is required to be less breathable than before under the high pressure, and to reduce the mesh shift of the sewing thread of the sewing part which comprises an airbag, and a fabric.

In view of this, for example, Japanese Unexamined Patent Publication No. 2950954 discloses an uncoated fabric using a yarn having a total fineness of 300 to 400 dtex. However, the sewing mesh in the patent is not sufficiently small. Japanese Unexamined Patent Application Publication No. 8-2359 discloses an airbag fabric which defines the amount of residual oil deposition and the lubrication resistance of the fabric in a fabric having a cover cover of 900-1400. Also in the publication, it is hard to say that it is enough to satisfy the sewing part mesh shift.

 U. S. Patent No. 5,073, 418 proposes a method of manufacturing a fabric with less than 500 denier yarns and rendering it in order to lower the air permeability by calendering, thereby improving the airtightness. There is a problem of falling.

EP 416483 discloses heat-shrinkable or heat-shrinkable nonwoven fabrics for the manufacture of airbags having a substantially symmetrical structure and characterized by a synthetic filament yarn having a denier of 300 to 400 dtex, but such a method is known as a synthetic filament yarn. In the process, the strength is sharply lowered, there is a problem that the tear strength of the fabric is lowered.

EP 436950 includes treating a fabric made of polyamide filament yarn at a temperature of 60 ° C. to 140 ° C. in an aqueous bath, with a hot air shrinkage of 6 to 15% at 160 ° C. and at least nearly symmetrical fabric structure. , But a method for producing an industrial fabric having a dense structure, which does not require coating treatment, but such a method is a synthetic filament yarn heat shrinkage rapidly in a high temperature aqueous bath, the fabric quality is degraded, the fabric tear strength Has a problem of falling.

An object of the present invention is the step of (A) weaving low shrinkage triangular cross-section polyamide fiber having a dry heat shrinkage (190 ℃, 15 minutes) of 3 to 6% with dough for airbag, (B) the dough by 5 to 20 ℃ (3) further heat contraction by sequentially passing three to ten aqueous baths of which the temperature rises, (C) passing the water bath through the steam heater, and (D) the steam heater It is an object of the present invention to provide a fabric for an uncovered air bag manufactured by a method comprising the step of passing the fabric passed through a hot air dryer.

In another aspect, the present invention by producing a dough for airbag using a low shrinkage triangular cross-section polyamide fiber for an uncovered airbag having a dry heat shrinkage (190 ℃, 15 minutes) of 3 to 6% obtained by more stably controlling the crystal structure of the stretched yarn High thermal shrinkage of the fabric, which is a problem of the prior art, can overcome the problem of poor quality, tensile strength and tear strength of the fabric.

The present invention comprises the steps of (A) weaving a low shrinkage triangular cross-section polyamide fiber having a dry heat shrinkage (190 ℃, 15 minutes) of 3 to 6% in the dough for air bags, (B) the dough by 5 to 20 ℃ sequentially Unshrinkable airbag manufactured by the method comprising the steps of continuously passing 3 to 10 aqueous baths of increasing temperature to heat shrink, and (C) passing the fabric passing through the steam heater through a hot air dryer. Provide the fabric for

In addition, further comprising the step of additional heat shrink by passing the fabric passed through the aqueous bath in step (B) through a steam heater.

In addition, the temperature of the steam heater is preferably 150 to 220 ℃.

In addition, in the step (B), it is preferable that the dough for the airbag first passes through the aqueous bath having a temperature of 50 ° C. and successively passes five aqueous baths in which the temperature rises by 10 ° C. in sequence.

In addition, the temperature of the fabric inlet port of the hot air dryer in the step (C) is 140 to 160 ℃ but the temperature of the fabric outlet is preferably set to about 30 to 70 ℃ higher than the temperature of the inlet.

The present invention provides a fabric for an uncovered airbag having a tensile strength of 200 to 300 kg, a tear strength of 25 to 40 kg, and an air permeability of 1.0 cm ³ / cm ² / sec or less.

The polyhexamethyleneadipamide polymer used in the present invention contains at least 85 mole% of hexamethyleneadipamide repeating units, and preferably consists only of hexamethyleneadipamide units.

Alternatively, any polyamide homopolymer and copolymer can be used in place of the polyhexamethyleneadipamide. Such polyamides are mainly aliphatic. Poly (hexamethylene adipamide) (nylon 66); Poly (e-caproamide) (nylon 6); And widely used nylon polymers such as copolymers thereof. Nylon 66 is most preferred. Other nylon polymers that can be advantageously used are nylon 12, nylon 46, nylon 6 · 10 and nylon 6 · 12.

The polyhexamethyleneadipamide chip according to the present invention may be added in an amount such that the residual amount of copper metal in the final polymer is 20 to 50 ppm in order to improve thermal stability. Pyrolysis occurs due to poor thermal stability, and when it is more than 50 ppm, more than necessary copper metal acts as a foreign matter, which is a problem in spinning.

The polyhexamethyleneadipamide chip is fiberized according to the method of the present invention, and FIG. 1 schematically illustrates a manufacturing process according to one embodiment of this invention.

The polyhexamethyleneadipamide chip was passed through a pack (1) and a nozzle (2) at a spinning temperature of preferably 270 to 310 ° C., preferably a spinning draft ratio of 20 to 200 (linear velocity on the first winding roller / By low temperature melt spinning at a linear velocity at the nozzle, it is possible to prevent a decrease in the viscosity of the polymer due to thermal decomposition. If the spinning draft ratio is less than 20, the uniformity of the filament cross section worsens, and the drawing workability is significantly lowered. If it exceeds 200, the filament breakage occurs during spinning, making it difficult to produce a normal yarn.

In addition, in this invention, it is an important factor to adjust the filtration residence time in a pack to 3-30 second. If the filtration residence time in the pack is less than 3 seconds, the filtration effect of the foreign matter is insufficient, and if it is more than 30 seconds, pyrolysis is severe due to excessive pack pressure increase.

In addition, in the present invention, it is preferable to set the L / D (length / diameter) of the extruder screw to 10 to 40, which is difficult to uniformly melt when the L / D of the screw is less than 10, and to exceed 40 due to excessive shear stress. Molecular weight fall is severe and physical property is inferior.

In the present invention, the melt-discharge yarn (4) is passed through the cooling zone (3) to quench and solidify. In the cooling zone 3, an open quenching method, a circular closed quenching method, and a radial outflow quenching method may be applied depending on a method of blowing cooling air. Open quenching is preferred. Subsequently, the discharged yarn 4 solidified while passing through the cooling zone 3 can be oiled by the emulsion applying device 5 to 0.5 to 1.0%.

The preferred spinning speed of the undrawn yarn is 200 to 1,000 m / min.

The yarn having passed through the first drawing roller 6 is drawn at a draw ratio of at least 4.0 times, preferably 4.5 to 6.5, while passing through the series of drawing rollers 7, 7, 8, 9 and 10 by a spin draw method. The final stretched yarn 11 is obtained by doing this.

In the present invention, the core of the technical configuration is that the dry heat shrinkage rate of the fiber (190 ° C., 15 minutes) is 3 to 6%. At this time, the shrinkage of the fiber has a value that varies depending on the measurement temperature, the dry heat shrinkage at 190 ℃, 15 minutes has a value of 1% higher than the value measured at 160 ℃, 30 minutes. That is, the shrinkage value measured at 160 ° C. for 30 minutes of the low shrinkage fiber manufactured according to the present invention is about 2 to 5%. The low shrinkage of such fibers is achieved by stabilizing the crystal structure of the stretched yarn in the heat treatment process after the two-stage stretching process. The multi-stage stretching process of the present invention consists of a primary stretching process proceeding at a high stretching ratio at a low stretching temperature and a secondary stretching process proceeding at a relatively low stretching ratio at a high temperature.

In the primary stretching step of the present invention, crystallization mainly by orientation proceeds. The crystallization by this orientation is a factor in determining the heat shrink in the fabric refining process. The preferred stretching temperature in the primary stretching process of the present invention is 20 to 50 ℃, the stretching ratio is 3.0 times or more, it is difficult to manage the stretching temperature is less than 20 ℃ without installing an additional cooling device in the stretching roller in the process. It is difficult and economically disadvantageous, and when the stretching temperature exceeds 50 ° C, crystallization by heat proceeds. Moreover, when the draw ratio is less than 3.0 times, sufficient orientation crystallization hardly occurs.

In the secondary stretching step of the present invention, crystallization by heat proceeds at a high temperature. The heat crystals at these high temperatures affect the heat shrinkage of the fabric in the hot air dryer, the drying process after refining. In the secondary stretching step of the present invention, the preferred stretching temperature is 200 to 250 ° C, and the draw ratio is 2.0 times or less. If the stretching temperature is less than 200 ° C, sufficient crystallization by heat does not proceed, and the stretching temperature exceeds 250 ° C. It causes damage to the yarn. In addition, when the draw ratio exceeds 2.0 times, the elongation of the yarn decreases drastically.

In the present invention, a key technical matter is to adjust the relaxation temperature to 200 to 250 ° C. and the relaxation rate to 3 to 7% in order to stabilize the crystal structure of the drawn yarn. The low shrinkage characteristics of the fiber can prevent the air bag dough from being rapidly thermally contracted in the refining and drying process, so that the quality of the fabric is good and the high utilization rate is high.

The low shrinkage triangular polyamide fibers produced according to the method of the present invention are (1) dry heat shrinkage of 3 to 6% (190 ° C., 15 minutes), (2) strength of 9.0 g / d or more, (3) 20% or more Elongation, (4) birefringence of 0.065 or less, and (5) 200 to 1000 denier.

Stretched polyhexamethyleneadipamide fibers produced by the present invention, using rapier or wortjet looms, 210 denier triangular polyamide yarns typically have 27-30 / cm yarn to achieve the required air permeability. Male, 420 denier yarns of 16 to 22 / cm in both warp and weft yarns, 630 denier yarns of 13 to 18 / cm in both warp and weft yarns are woven in plain weave.

In the present invention, the woven fabric is preferably woven into a plain weave having a symmetrical structure. However, in order to obtain an attractive woven fabric, a yarn having a thinner linear density may be woven into a 2/2 Panama weave of a symmetrical structure.

The key technical features of the present invention are characterized by a process of heat shrinking in multiple stages in the dough for airbag manufactured by the above-described method, in a steam heater and a hot air dryer.

In the refining process of the present invention, the dough for airbags first passes through an aqueous bath having a temperature of 50 ° C. and sequentially passes three to six aqueous baths whose temperature rises in steps of 10 to 20 ° C. sequentially. At this time, the temperature of the final aqueous bath is 100 ℃.

Another feature of the present invention is to further heat shrink by passing the fabric subjected to heat shrink after the refining process through a hot air dryer. At this time, the temperature of the hot air dryer is 150 to 220 ℃.

In the present invention, the key technology is to further shrink the fabric by using a steam heater of 150 to 220 ℃ continuously after the refining process. This is because the low shrinkage triangular polyamide fibers produced according to the present invention are difficult to ensure sufficiently low air permeability required for airbags only by shrinking of the fabric occurring in the refining and drying process. At this time, the heat shrink ratio of the fabric by the steam heater is preferably about 10 to 40% relative to the heat shrink of the entire fabric.

As described above, in the present invention, by using the low-shrink fiber as the fabric for the air bag, it is possible to prevent the damage of the fabric due to the rapid shrinking of the fabric in the refining process and the hot air dryer, and to improve the strong utilization of the fabric.

Hereinafter, the present invention will be described in more detail based on the following examples. However, the following examples are not intended to limit the present invention, but are not limited thereto. Various physical property evaluations of the yarns and treatment cords prepared in Examples and Comparative Examples of the present invention were performed by the following methods.

(1) Relative viscosity (I.V.)

After dissolving 0.1 g of sample in sulfuric acid (90%) for 90 minutes to make the concentration 0.4g / 100ml, transfer to Ubbelohde viscometer, hold for 10 minutes in 30 ℃ thermostat, use viscometer and aspirator The number of seconds of the drop of the solution was calculated | required. The number of falling seconds of the solvent was also determined in the same manner, and then the R.V. value was calculated by the following equation.

(2) strength

Sample length of 250 mm, 300 mm / min after leaving at least 24 hours under standard conditions (20 ° C., 65% relative humidity) according to ASTM D 885, using Instron 5565 (manufactured by Instron, USA) The elongation was measured under the conditions of the tensile speed and 20 turns / m.

(3) non-shrinkage rate

The sample was left at 20 ° C. and 65% relative humidity for at least 24 hours, and then weighed to a weight of 0.1 g / d to measure the length (L 0), and treated in boiling water at 100 ° C. for 30 minutes under no tension. Next, taken out and left for 4 hours or more, the load was measured and the length (L) was measured, and the shrinkage ratio was calculated by the following equation.

(4) dry heat shrinkage

The sample was left at 20 ° C. and 65% relative humidity for at least 24 hours, and then weighed at a weight of 0.1 g / d to measure the length (L 0), followed by 15 minutes at 190 ° C. using a dry oven under no tension. After the treatment was taken out and left for 4 hours or more, the load (L) was measured, and the shrinkage ratio was calculated by the following equation.

(5) degree of release of fiber

The degree of release is the ratio of the circumscribed circle diameter (a) to the inscribed circle diameter (b).

(6) tensile strength of fabric

Using Instron 4465 (manufactured by Instron, USA), the fabric was allowed to stand for 10 hours or more in a standard condition (20 ° C., 65% relative humidity) according to ASTM D 5034. The tensile strength of the fabric was measured.

(7) tear strength of fabric

Tear steel of fabric using Instron 4465 (manufactured by Instron, USA) for at least 24 hours under standard conditions (20 ° C, 65% relative humidity) according to the tongue method under ASDM D 2261. The degree was measured.

(8) air permeability of fabric

Using a Frazier air permeability meter, the air permeability of the fabric was measured under 125 Pa pressure according to the ASDM 737 method.

Example 1

A polyhexamethyleneadipamide chip having a relative viscosity (RV) 3.4 containing 40 ppm each of copper metal was melt-spun using an extruder at a spinning draft ratio of 40 at a temperature of 296 ° C. to draw undrawn yarn having a triangular cross section. At this time, the filtration residence time in the pack was 17 seconds, the screw of the extruder used had an L / D of 35, and a static mixer having two units was installed in the polymer conduit of the pack to evenly mix the melt-spun polymer. The discharge yarn was then solidified through a 600 mm long cooling zone (20 ° C., cooling air blow with a wind speed of 0.5 m / sec) and then oiled with a spinning emulsion. This undrawn yarn was wound at a spinning speed of 470 m / min and stretched in two stages. The first stage stretching is performed 3.5 times at 30 ° C., the second stage stretching is 1.6 times at 223 ° C., the heat setting (relaxation temperature) at 235 ° C., 6% relaxation, and then wound to give the final drawn yarn of 630d / 136f denier. Prepared.

The physical properties of the stretched yarn thus prepared are shown in Table 1 below.

[Examples 2 to 6 and Comparative Examples 1 to 12]

As shown in Table 1, a stretched yarn was prepared by performing experiments in the same manner as in Example 1 while changing the cross-sectional shape, fineness, spinning temperature, and stretching conditions.

The physical properties of the drawn yarn thus obtained were evaluated and shown in Table 1 below.

TABLE 1

division Chip relative viscosity Spinning temperature (℃) Island Relaxation conditions Drawing company Relaxation temperature (℃) % Relaxation Dry Heat Shrinkage (%) (190 ℃ × 15min) Non-shrinkage rate (%) Shape Strength (g / d) Elongation (%) Example 1 3.4 296 630d / 136f 235 6.0 5.2 5.6 1.5 8.8 22.1 Example 2 3.4 296 630d / 100f 235 6.0 4.6 5.2 1.5 8.9 22.1 Example 3 3.4 296 420d / 68f 235 6.0 4.4 5.1 1.5 9.0 22.6 Example 4 3.4 296 420d / 136f 235 6.0 5.6 5.9 1.5 9.1 24.4 Example 5 3.4 296 210d / 34f 235 6.0 5.1 5.6 1.5 9.2 24.6 Example 6 3.4 296 210d / 68f 235 6.0 5.6 5.8 1.5 9.2 23.4 Comparative Example 1 3.4 296 630d / 136f 225 6.0 5.8 6.2 1.0 (round section) 9.2 25.1 Comparative Example 2 3.4 296 630d / 100f 225 6.0 5.8 6.2 1.0 (round section) 9.2 24.1 Comparative Example 3 3.4 296 420d / 68f 225 6.0 5.4 5.8 1.0 (round section) 9.2 24.6 Comparative Example 4 3.4 296 420d / 136f 225 6.0 6.2 6.6 1.0 (round section) 9.6 24.4 Comparative Example 5 3.4 296 210d / 34f 225 6.0 5.4 5.8 1.0 (round section) 9.2 24.6 Comparative Example 6 3.4 296 210d / 68f 225 6.0 6.2 6.6 1.0 (round section) 9.6 25.4 Comparative Example 7 3.4 296 630d / 136f 205 2.0 7.8 8.2 1.0 (round section) 9.4 22.1 Comparative Example 8 3.4 296 630d / 100f 205 2.0 7.8 8.2 1.0 (round section) 9.4 21.1 Comparative Example 9 3.4 296 420d / 68f 205 2.0 7.4 7.8 1.0 (round section) 9.4 21.6 Comparative Example 10 3.4 296 420d / 136f 205 2.0 8.2 8.6 1.0 (round section) 9.8 21.4 Comparative Example 11 3.4 296 210d / 34f 205 2.0 7.4 7.8 1.0 (round section) 9.4 21.6 Comparative Example 12 3.4 296 210d / 68f 205 2.0 8.2 8.6 1.0 (round section) 9.4 22.4

Example 7

The low shrinkage triangular yarn prepared in Example 3 was flattened to a fabric of 49x49 per inch with a rapier loom to prepare dough for airbags. The dough is first passed through an aqueous bath of 50 ° C., and successively passes through five aqueous baths in which the temperature is sequentially increased by 10 ° C. At this time, the temperature of the final aqueous bath is 100 ℃. Further heat shrinkage is carried out by passing the fabric through a steam heater after the refining process. At this time, the temperature of the steam heater is 180 ℃. The fabric passed through the steam heater is dried in a hot air dryer at 180 ℃.

Evaluation of the physical properties of the fabric thus prepared is shown in Table 2 below.

Comparative Example 13

The low-shrink circular cross-section yarn prepared in Comparative Example 3 was flattened to a fabric of 49x49 per inch by a rapier loom to prepare dough for airbags. The dough is first passed through an aqueous bath of 50 ° C., and successively passes through five aqueous baths in which the temperature is sequentially increased by 10 ° C. At this time, the temperature of the final aqueous bath is 100 ℃. After the refining process, additional heat shrinkage is carried out by passing the fabric through a steam heater. At this time, the temperature of the steam heater is 190 ℃. The fabric passed through the steam heater is dried in a 180 ° C. hot air dryer.

Evaluation of the physical properties of the fabric thus prepared is shown in Table 2 below.

Comparative Example 14

The high shrink circular cross-section yarn prepared in Comparative Example 9 was flattened to a fabric of 49x49 per inch by a rapier loom to prepare dough for airbags. The dough is first passed through an aqueous bath of 50 ° C., and successively passes through five aqueous baths in which the temperature is sequentially increased by 10 ° C. At this time, the temperature of the final aqueous bath is 100 ℃. After the refining process, additional heat shrinkage is carried out by passing the fabric through a steam heater. At this time, the temperature of the steam heater is 190 ℃. The fabric passed through the steam heater is dried in a hot air dryer at 180 ℃.

Evaluation of the physical properties of the fabric thus prepared is shown in Table 2 below.

Comparative Example 15

The yarn prepared in Example 3 was flattened to a fabric of 49x49 per inch with a rapier loom to prepare dough for airbags. The dough is rapidly thermally contracted by passing it through an aqueous bath at 95 ° C., and then dried in a 180 ° C. hot air dryer.

Evaluation of the physical properties of the fabric thus prepared is shown in Table 2 below.

[Comparative Example 16]

The yarn prepared in Example 3 was flattened to a fabric of 49x49 per inch with a rapier loom to prepare dough for airbags. The dough was thermally contracted using a calendaring apparatus at 180 ° C. at a pressure of 483 kilopascals to prepare a fabric.

Evaluation of the physical properties of the fabric thus prepared is shown in Table 2 below.

TABLE 2

division Yarn island Fabric Density (Bon / Inch) Tensile strength (㎏) Tear strength (㎏) Thickness (mm) Air permeability (cm ³ / cm ² / sec) Weight (g / ㎡) Example 7 420d / 68f 49 × 49 229 × 221 27.5 × 26.3 0.36 0.4 236 Comparative Example 13 420d / 68f 49 × 49 228 × 223 28.5 × 25.3 0.39 0.8 235 Comparative Example 14 420d / 68f 49 × 49 192 × 183 20.5 × 19.3 0.40 0.6 241 Comparative Example 15 420d / 68f 49 × 49 201 × 191 17.5 × 16.3 0.36 1.3 236 Comparative Example 16 420d / 68f 49 × 49 195 × 178 16.5 × 16.1 0.3.8 1.4 236

As shown in Table 2, when the low shrinkage triangular yarn of the present invention (Example 7) is used, it is possible to secure lower breathability of the fabric than the low shrinkage circular cross-section yarn (Comparative Example 13), and the conventional high shrinkage circular cross-section If yarn (Comparative Example 14) is used, low air permeability can be secured, but the tensile strength and tear strength drop sharply due to excessive shrinkage of the fabric. In addition, when the heat shrinkage of the fabric is slowly progressed in multiple stages according to the present invention (Example 7), the tensile strength and tear strength are much better than those of the rapid thermal shrinkage of the fabric (Comparative Example 15, Comparative Example 16).

As described above, the present invention uses a low shrinkage triangular cross-section polyamide fiber for an uncovered airbag having a dry heat shrinkage ratio (190 ° C., 15 minutes) of 3 to 6%, which is obtained by controlling the crystal structure of the stretched yarn more stably, for the airbag dough. By manufacturing the high heat shrinkage of the fabric, which is a problem of the prior art, the quality of the fabric is lowered, it can be prevented that the tensile strength and tear strength of the fabric falls. Because of this, fabrics for airbags made from the fibers of the present invention are excellent in grade, tensile strength and tear strength, and have low breathability.

1 is a process schematic diagram illustrating a spinning process of a low shrink triangular cross-section polyamide fiber of the present invention.

Figure 2 is an example of an enlarged cross-sectional view of the triangular cross-section yarn produced by the present invention

Claims (6)

(A) weaving a low shrinkage triangular cross-section polyamide fiber having a dry heat shrinkage (190 DEG C, 15 minutes) of 3 to 6% into a dough for airbags, (B) heat shrinking the dough by successively passing three to ten aqueous baths in which the temperature is sequentially increased by 5 to 20 ° C., (C) The fabric for the uncoated airbag manufactured by the method comprising the step of passing the fabric passed through the steam heater through a hot air dryer. The method of claim 1, Fabric for passing through the aqueous bath in step (B) further comprises the step of heat-shrinkable by passing through a steam heater for a non-covered air bag fabrics. The method of claim 2, The temperature of the steam heater is a non-covered air bag fabric, characterized in that 150 to 220 ℃. The method of claim 1, The fabric for the uncovered airbag of step (B), wherein the dough for the airbag first passes the aqueous bath having a temperature of 50 ° C. and sequentially passes five aqueous baths in which the temperature rises by 10 ° C. sequentially. The method of claim 1, The fabric inlet temperature of the hot air dryer in the step (C) is 140 to 160 ℃ but the temperature of the fabric outlet is set to about 30 to 70 ℃ higher than the temperature of the inlet fabric, characterized in that for fabric. The method of claim 1 The uncoated airbag fabric has a tensile strength of 200 to 300kg, tear strength 25 to 40kg, air permeability of 1.0 cm ³ / cm ² / sec or less, characterized in that the fabric for uncoated air bags.