JP2008156808A - Rectangular spinning pack and method for spinning synthetic fibers using the rectangular spinning pack - Google Patents

Abstract

<P>PROBLEM TO BE SOLVED: To provide a rectangular spinning pack with which occurrence of yarn breakages and irregularities in quality of a spun yarn can be reduced by optimizing the shape of a polymer flow passage with a simple structure to eliminate remaining air, and a method for spinning synthetic fibers. <P>SOLUTION: The spinning pack is disposed with a filter material, a porus plate and a spinneret having rectangular arrangement of holes viewed from the upper face in a lower pack case in this order in the entire flow direction of a spun polymer, and the filter material, the porus plate, and the spinneret are integrally assembled with an upper pack case. The upper pack case has the polymer flow passage having a rectangular cross sectional shape, when a cross section perpendicular to the entire flow of the polymer is viewed. While the inclination of a wall surface of the polymer flow passage is gently widen toward the downstream, when a cross section passing through the axis of the spinning pack and parallel to the entire flow of the polymer is viewed. <P>COPYRIGHT: (C)2008,JPO&INPIT

Description

  The present invention relates to a rectangular spinning pack for synthetic fibers and a method for spinning synthetic fibers. More specifically, the present invention relates to a rectangular spinning pack for improving air remaining and polymer discharge spots in a pack into which a polymer flows, and the pack. The present invention relates to a method for spinning synthetic fibers using

In general, a round spinning pack shown in FIG. 3 is widely used as a spinning pack used for spinning synthetic fibers. In the lower pack case 5, a filter medium 2 and a filter medium 2 are arranged in the direction of the entire flow of the polymer to be spun. The perforated plate 3 and a base 4 having a circular shape when viewed from above are arranged, and the filter medium 2, perforated plate 3 and base 4 are assembled together in an upper pack case 1 having a polymer inflow pipe 6. Configured. The upper pack case 1, as shown in FIG. 4, when viewed cross-section perpendicular to the polymer stream, the cross section has a polymer flow passage F ₁ is circular, polymers, not shown polymer feed It is introduced into the polymer inflow pipe 6 provided in the upper pack case 1 from the pipe, and is spun from the base 4 through the filter medium 2 and the perforated plate 3.

  So far, the round spinning pack has been proposed as an appropriate wall shape of the upper pack case, for example, as a countermeasure against problems such as yarn breakage due to abnormal retention of the polymer and yarn-like quality spots (see, for example, Patent Document 1), Further, it has been proposed to prevent abnormal stagnation at the inner end of the spin pack case by making the upper pack case end into an arc shape (see, for example, Patent Document 2), and optimizing the flow in the round spin pack. Measures have been taken.

  However, in recent years, with the trend of increasing the size of production machines due to productivity improvement, there is an increasing need for a rectangular base that can increase the number of base holes. Among them, a rectangular spinning pack having the structure shown in FIG. 5 is known as a rectangular spinning pack used for spinning synthetic fibers. This rectangular spinning pack technology has the following drawbacks.

In the rectangular spinning pack, the polymer flows from the polymer inflow pipe 6 to the filter medium through the polymer flow path F ₁ that connects the outflow surface of the polymer inflow pipe 6 in the upper pack case 1 and the lower end of the upper pack case in a straight line. However, in the cross section orthogonal to the whole polymer flow, as shown in FIG. 6, each distance from the center of the cross section to the wall surface is non-uniform, so that the flowed polymer reaches the wall surface in the cross section. The time is different. For this reason, regions with different polymer residence times are created in the upper pack case 1, and in the regions where the polymer residence time is long, the polymer is deteriorated and the yarn is likely to break, and the quality unevenness such as the occurrence of patches on the thickness. There was a problem that caused

  Further, in the polymer flow path, the variation in the polymer flow rate is large, and air tends to remain in the portion where the flow rate is slow, and yarn breakage occurs due to the outflow of the remaining air.

For these problems, the technology of the above-mentioned patent document is a technical content limited to a round spin pack. If the above-mentioned patent document 1 is applied to the upper pack case of a rectangular spin pack, the upper part as shown in FIG. A wall is formed at the end of the pack case in a direction parallel to the entire polymer flow, and abnormal retention of the polymer tends to occur at the end of the upper pack case. In particular, in the short side direction, the wall becomes high, so air tends to remain, and the polymer flow cannot be optimized. Further, although it has been proposed to optimize the flow to the end of the upper pack case of the spinning pack using a perforated plate capable of guiding the polymer in the outer peripheral direction (see, for example, Patent Document 3), The polymer flow path connects the outflow surface of the polymer inflow pipe in the case and the lower end of the upper pack case in a straight line, creating a region where air tends to remain, and can be applied because yarn breakage occurs due to the outflow of residual air. Therefore, the above problem has not been solved.
JP-A-6-264304 JP 2000-017517 A JP 2003-342826 A

  The object of the present invention is to solve the above-mentioned conventional problems, and by optimizing the shape of the flow path of the polymer with a simple structure, the remaining of air is eliminated, occurrence of yarn breakage, spinning An object of the present invention is to provide a rectangular spinning pack and a synthetic fiber spinning method capable of reducing unevenness in yarn quality.

The present invention for solving the above-described problems has one of the following configurations. That is,
(1) In the lower pack case, a filter medium, a perforated plate, and a base having a rectangular hole arrangement as viewed from above are arranged in this order in the direction of the entire flow of the polymer to be spun. And a perforated plate and a base are integrally assembled in an upper pack case, and the upper pack case is a polymer channel whose cross-sectional shape is rectangular when viewed in a cross section perpendicular to the entire polymer flow. A rectangular shape characterized in that when viewed in a cross section passing through the central axis of the spin pack and parallel to the entire polymer flow, the inclination of the wall surface of the polymer flow path becomes gentler as it goes downstream. Spinning pack.

  (2) In the polymer flow path, the center axis of the spin pack is the z axis with the polymer flow direction being negative, and the point where the z axis intersects the upper pack case outflow surface is the origin, and the upper pack case outflow surface passes through the origin. The direction parallel to one side is the x axis, the direction passing through the origin and perpendicular to the x axis is the y axis, the distance from the upper pack case outflow surface to the polymer inflow tube outflow surface is L, and the polymer inflow tube radius is r. The cross section of the polymer channel perpendicular to the axis is the following formula (1)

The rectangular spinning pack according to (1), wherein the rectangular spinning pack is a rectangle having a point satisfying the above as a central value and having a vertex within a range of ± 15%.
Where X ₁ is ½ of the length of one side in the x-axis direction on the outflow surface of the upper pack case
Y ₁ : 1/2 of one side length in the y-axis direction on the outflow surface of the upper pack case
(3) In the polymer flow path, the center axis of the spin pack is the z axis with the polymer flow direction being negative, and the point where the z axis intersects the upper pack case outflow surface is the origin, and the upper pack case outflow surface passes through the origin. The direction parallel to one side is the x axis, the direction passing through the origin and perpendicular to the x axis is the y axis, the distance from the upper pack case outflow surface to the polymer inflow tube outflow surface is L, the polymer inflow tube radius is r, the polymer flow When the path is divided into n _max stages in the z-axis direction with z = 0 as the first stage, the cross section of the polymer flow channel orthogonal to the n-th stage z axis where z = z _n is expressed by the following formula (1)

It has a rectangle having an apex at the central value and to the range of ± 15% of the points which satisfy the the respective sides of a rectangular n-th cross-section that the polymer flow path wall at _{z = z n, z = z} n + 1 The rectangular spinning pack according to claim 1, wherein each of the rectangular sides of the (n + 1) -th stage cross section is a plane connected by a straight line.
Where X ₁ is ½ of the length of one side in the x-axis direction on the outflow surface of the upper pack case
Y ₁ : 1/2 of one side length in the y-axis direction on the outflow surface of the upper pack case
(4) A synthetic fiber spinning method, comprising spinning using the rectangular spinning pack according to any one of (1) to (3).

  According to the rectangular spinning pack of the present invention, the polymer flow path can be optimized. Accordingly, air remaining in the pack and polymer discharge spots can be prevented, and stable spinning can be performed, quality deterioration can be prevented, and quality and productivity can be greatly improved.

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

FIG. 1 is a cross-sectional view parallel to polymer flow showing one embodiment of a rectangular spin pack according to the present invention. In FIG. 1, in the lower pack case 5, a filter medium 2, a perforated plate 3, and a base 4 having a rectangular hole arrangement as viewed from above are arranged in this order in the direction of the entire flow of the polymer to be spun. The material 2, the perforated plate 3, and the base 4 are integrally assembled in the upper pack case 1 having the polymer inflow pipe 6. The upper pack case 1 has a rectangular cross section when viewed in a cross section orthogonal to the polymer flow, and passes through the central axis of the spin pack, and when viewed in a cross section parallel to the entire polymer flow, the inclination of the wall forms a flared polymer flow passage F ₁ becomes gentler as the go downstream. Reference numeral 7 denotes a packing for preventing the members from coming into direct contact during assembly or preventing the polymer from flowing out, and reference numeral 8 denotes an assembly bolt.

  In the above, the filter medium 2 is a wire mesh or a non-woven fabric, and removes foreign matters in the polymer that cause a problem in spinning, and has a relatively large flow resistance and functions to uniformly disperse the polymer. Have. The perforated plate 3 supports the filter medium.

The general overall flow of the polymer in the spinneret pack will be described. The polymer flows from the upstream process (not shown) through the polymer supply pipe to the polymer inflow pipe 6 provided for inflowing the polymer into the upper pack case 1. After passing through the polymer flow path F ₁ , foreign matter is removed by the filter medium 2, and then reaches the base 4 through the perforated plate 3 and is discharged from the base 4 to become a thread. That is, it is spun.

Next, a description will be given polymer flow passage F ₁ shape.

7-9 shows a three-view drawing of the polymer flow path F ₁ of the upper pack case 1 in the rectangular spin pack according to the present invention. The polymer flow path F ₁ is for the polymer supplied from the polymer inflow pipe 6 to expand in a direction orthogonal to the entire polymer flow, and the cross-sectional shape orthogonal to the entire polymer flow has a polymer flow. because the outflow surface of the road-F ₁ is rectangular, also it has a rectangular cross-sectional shape orthogonal to the entire polymer stream. In addition, the polymer flow path F ₁ has a divergent shape in which the inclination of the wall surface of the polymer flow path becomes gentler as it goes downstream, when a cross section passing through the central axis of the spinning pack and parallel to the entire polymer flow is viewed. By adopting such a shape, the polymer can easily flow along the wall surface. Therefore, the direction of the overall flow is compared with the flow path shape in which the outflow surface of the polymer inflow pipe 6 and the lower end of the upper pack case are simply connected in a straight line. The polymer can be expanded in a direction orthogonal to the polymer, and the polymer residence time in the spin pack becomes uniform. Here, the outflow surface of the polymer flow path F ₁ is hereinafter referred to as the outflow surface of the upper pack case 1, and includes one in which the outer peripheral portion is rounded, the inflow surface into the polymer flow path F ₁ and the polymer inflow pipe 6. The boundary surface is hereinafter referred to as the outflow surface of the polymer inflow pipe 6, and the outer peripheral portion is rounded.

  And when the cross section orthogonal to the whole polymer flow is seen, it is preferable that the shape of this wall surface has a rectangle which has each vertex which satisfies the following formula.

7 to 9, the center axis of the rectangular spinning pack is the z-axis with the polymer flow direction negative, and the point where the z-axis and the outflow surface of the upper pack case 1 intersect is the origin, and the outflow surface of the upper pack case 1 passes through the origin. The direction parallel to one side is the x axis, the direction passing through the origin and perpendicular to the x axis is the y axis, the distance from the outflow surface of the upper pack case 1 to the outflow surface of the polymer inflow pipe 6 is L, and the polymer inflow pipe radius is Assume that ½ of the side length in the x-axis direction on the rectangular surface at r, z = 0 is X ₁ , and ½ of the side length in the y-axis direction of the rectangular surface at z = 0 is Y ₁ .

  Here, for the polymer flow path, the inclination of the wall surface of the polymer flow path suddenly becomes gentle in the vicinity of the outflow surface of the upper pack case 1 as shown in FIG. 8, or as shown in FIG. Even if the angle of the polymer channel gradually decreases, as long as the slope of the wall of the polymer flow path becomes gentler as it goes downstream, the polymer can easily flow along the wall surface. Although it is possible to easily spread in the orthogonal direction and to reduce abnormal stagnation of the polymer, the points on the outflow surface of the polymer inflow pipe 6 and the points on the outflow surface of the upper pack case 1 as shown in FIG. The cross section of the orthogonal polymer flow path at an arbitrary height z is expressed by the following formula (1).

When the rectangular cross-section with the point satisfying the above is a vertex, each side of the rectangular cross-sectional shape is multiplied by an equal ratio, so the polymer flow path is seen from the polymer inflow pipe in the x-y cross section in the x and y directions. This is more effective because the polymer can be easily spread at a constant rate in a direction orthogonal to the entire flow. Here, in FIG. 8 and FIG. 9, the wall surface derived | led-out from Formula (1) is shown with the dotted line for reference. Even if the vertices of the rectangular cross section do not exactly match the formula (1), it is practically sufficient if the rectangle having a vertex within the range of ± 15% with the value of the formula (1) as the center value is used. An effect can be obtained. FIG. 10 shows the result of adding a virtual wall surface having a vertex at the value + 15% of the equation (1) and a virtual wall surface having a vertex at the value −15% of the equation (1).

  In addition, a polymer flow path that satisfies the above formula (1) is preferable, but it is complicated to machine and manufacture the curved surface as described above. Therefore, a rectangular surface orthogonal to the entire polymer flow is divided into several stages. It is good also as a flow path shape which is created and expands stepwise and linearly. Producing a rectangular surface in several steps not only provides the same effect as an upper pack case with a polymer flow path that satisfies the above formula, but also ensures proper polymer flow without requiring complex processing. The upper pack case can be finished.

An example of the shape at this time will be described in more detail. In FIG. 2, the central axis of the rectangular spinning pack is the z-axis with the polymer flow direction negative, and the point where the z-axis intersects the outflow surface of the upper pack case 1 is the origin, and one side of the outflow surface of the upper pack case 1 passes through the origin. The direction parallel to the x axis, the direction passing through the origin and perpendicular to the x axis is the y axis, the distance from the outflow surface of the upper pack case 1 to the outflow surface of the polymer inflow tube 6 is L, the polymer inflow tube radius is r, X ₁ is ½ of the side length in the x-axis direction of the rectangular surface at z = 0, and Y ₁ is ½ of the side length in the y-axis direction of the rectangular surface at z = 0.

Now, from the outflow surface of the upper pack case 1 to the outflow surface of the polymer inlet pipe 6 the height L, and is divided into n _max stage in the z-axis direction z = 0 as a first stage, a z = z _n n The cross section of the polymer channel perpendicular to the z-axis of the step is expressed by the following formula (1)

A rectangle with each vertex satisfying. Then, the n-th rectangular sides is z = _{z n,} which is _{z = z n + 1 (n} + 1) sides of the rectangular stage are connected by a straight line, for further _{n max-th} stage, the polymer flows By making the same shape as the outflow surface of the pipe 6 and smoothly connecting with the (n _max −1) _-stage rectangle, the shape of the polymer channel wall surface can be made similar to the curved surface. In addition, n is a natural number of 2 or more, and is preferably 5 or more in order to bring the polymer flow path wall close to the curved surface, and the upper limit is not limited, but is preferably n in order to facilitate machining. = 12 or less is preferable.

  Here, it is more preferable that each step height is divided so as to be equal, but it is not always necessary to be divided equally, and each step height becomes narrower as it goes downstream in the polymer flow path, or Even if the width is increased, a sufficient effect can be obtained as long as the cross-sectional shape orthogonal to the z-axis is a rectangle having each vertex satisfying the formula (1).

  Further, the vertices of the rectangles in the respective steps are not necessarily exactly the values of the above formula, and the above formula (1) is used to make the coordinate value a natural number or a value that is easy to manufacture. A sufficient effect can be obtained by setting the value within a range of ± 15% of the value centering around ().

  Moreover, it is preferable that each ridgeline of a polymer flow path has smooth roundness, and the rectangular cross section in this invention shall also include the rectangle which rounded such a corner | angular part. Further, the roundness of the ridgeline is preferably in the range of R1 mm to R10 mm, and within this range, the cross-sectional shape of the polymer channel can be regarded as a rectangle, and the flow may be disturbed at the corners of the ridgeline. Not preferred.

  The rectangular spinning pack of the present invention is particularly useful for spinning high-viscosity thermoplastic resins. Furthermore, it is particularly effective for a polymer having a viscosity of 50 to 50,000 poise. By using the rectangular spinning pack of the present invention, air is not left in the pack, and yarn breakage and unevenness in the thickness of the yarn are eliminated. Stable spinning is possible without waking up.

Hereinafter, the effects of the present invention will be specifically described with reference to examples, but the embodiments according to the present invention are not limited to the examples. In this example, a steady flow analysis was performed on the polymer flow in the upper pack case using a numerical analysis tool (manufacturer: CD-adapco, analysis software: STAR-CD) for the flow velocity distribution in the spin pack.
(Example 1)
In the rectangular spinning pack using the upper pack case having the polymer flow path of the present invention shown in FIG. 1, the filter medium 2, the porous plate 3, and the base 4 are simulated as a porous medium, and the pressure loss ΔP applied to the porous medium Is the following formula (2) to which the Ergun equation is applied.

Further, the flow velocity v passing through the porous medium and the transmission coefficients α and β are derived. In this case, α is a coefficient of a term proportional to the square of the flow velocity v passing through the porous medium, and β is a coefficient of a term proportional to the flow velocity v passing through the porous medium. t is the thickness of the porous medium, and the thickness t of each porous medium is 1 mm for the filter medium 2, 25 mm for the porous plate 3, and 9 mm for the base 4. The permeation coefficient of each porous medium is α: 1.0 × 10 ⁻⁵ kg / m ⁴ and β: 1.0 × 10 ¹² kg / m ³ s for the filter medium 2, and α: 9 for the porous plate 3. .3 × 10 ⁷ kg / m ⁴ , β: 6.5 × 10 ⁸ kg / m ³ s, with base 4 α: 1.3 × 10 ¹¹ kg / m ⁴ , β: 1.7 × 10 ¹¹ kg / m ³ s. In addition, in order to simplify the calculation, numerical analysis is performed on a quarter-symmetric shape of the rectangular spinning pack, and the upper pack case at this time is equally divided into five stages. = 8 mm, L = 40 mm, X ₁ = 160 mm, and Y ₁ = 40 mm. As such spinning dope, a solution having a density of 1085 kg / m ³ and a viscosity coefficient of 112.2 kg / ms is used as the polymer stock solution, and the flow rate distribution in the upper pack case when the polymer is flowed at a flow rate of 16 m ³ / hr. The range where the polymer flow has a component with a flow rate of 0.005 m / s or more is indicated by hatching. The results obtained at this time are shown in FIG. As shown in FIG. 12, it was confirmed that the range where the flow velocity was 0.005 m / s or more (the range indicated by the hatched portion, the same applies to the following examples and comparative examples) extends to the end in the upper pack case. Therefore, if this base pack is applied, the polymer can easily reach the corner in the upper pack case, the location where the polymer tends to stay is eliminated, and there is no area where air tends to remain, so it is very good. It is thought that it will become a result.
(Example 2)
Numerical analysis was performed using the same conditions as in Example 1 except that the shape of the upper pack case was changed to a form that was not divided into multiple stages in the z-axis direction as shown in FIG. The obtained results are shown in FIG. 13 (the range in which the polymer flow has a component having a flow rate of 0.005 m / s or more is indicated by the hatched portion in the same manner as in Example 1). Very good results were obtained as in Example 1.
(Example 3)
Example 1 except that the value of x, y, z in the equation (1) shown in FIG. 10 is changed to a value of + 15% (excluding z = 0 and z = L) as the upper pack case. Numerical analysis was performed using the same conditions as those described above. The obtained result is shown in FIG. As in Example 1, good results were obtained.
Example 4
Example except that each value of x, y, z in the formula (1) shown in FIG. 10 is changed to a value of −15% (excluding z = 0 and z = L) as the upper pack case. Numerical analysis was performed using the same conditions as in 1. The obtained result is shown in FIG. As in Example 1, good results were obtained.
(Example 5)
Numerical analysis was performed using the same conditions as in Example 1 except that the upper pack case was changed to a form in which the wall surface of the polymer flow path suddenly became gentle as shown in FIG. The obtained results are shown in FIG. When the polymer flow path wall suddenly becomes gentle, the polymer tends to flow along the polymer flow path wall, so that there is no region where air easily remains, but the polymer is less likely to spread to the end as compared with Example 1. Therefore, the result that the area | region which can arrange | position the discharge hole in a nozzle | cap | die is somewhat limited was obtained. From these results, it was found that although it is necessary to pay attention to the arrangement of the discharge holes of the die in use, it can be used satisfactorily.
(Example 6)
Numerical analysis was performed using the same conditions as in Example 1 except that the upper pack case was changed to a form in which the wall surface of the polymer flow path gradually became gentle as shown in FIG. The obtained result is shown in FIG. When the polymer channel wall surface becomes gradually smaller, the polymer tends to spread to the end as compared with Example 5, but there is a portion where the polymer does not easily flow along the polymer channel wall surface particularly in the short side direction. As a result, a region in which the discharge holes are likely to remain is generated, and the region in which the discharge holes in the base can be arranged is somewhat limited. From these results, it was found that although it is necessary to pay attention to the arrangement of the discharge holes of the die in use, it can be used satisfactorily.
(Example 7)
Except that the upper pack case is replaced with a format in which the values of x, y, and z in the expression (1) shown in FIG. 11 are set to + 20% (excluding z = 0 and z = L), Numerical analysis was performed using the same conditions as in Example 2. The obtained result is shown in FIG. The obtained results are compared with the type in which the upper pack case of Example 3 is set to a value of + 15% of the value of the formula (1) shown in FIG. Since it remained easily, the result that the area | region which can arrange | position the discharge hole in a nozzle | cap | die was somewhat limited was obtained. From these results, it was found that although it is necessary to pay attention to the arrangement of the discharge holes of the die in use, it can be used satisfactorily.
(Example 8)
11 except that the upper pack case is changed to a format in which the values of x, y, and z in the formula (1) shown in FIG. 11 are set to −20% (except for z = 0 and z = L). Numerical analysis was performed using the same conditions as in Example 2. The obtained result is shown in FIG. The obtained results are compared with the case where the upper pack case of Example 4 is set to a value of −15% of the value of the formula (1) shown in FIG. As a result, the region where the discharge holes can be arranged in the die is somewhat limited. From these results, it was found that although it is necessary to pay attention to the arrangement of the discharge holes of the die in use, it can be used satisfactorily.
(Comparative Example 1)
A numerical analysis was performed using the same conditions as in Example 1 except that the shape of the conventional upper pack case that monotonously expands from the polymer inflow pipe outflow surface to the upper pack case outflow surface shown in FIG. . The obtained result is shown in FIG. 20 (the range in which the polymer flow has a component having a flow rate of 0.005 m / s or more is indicated by the hatched portion in the same manner as in Example 1). As shown in FIG. 20, in the conventional upper pack case, it can be seen that the polymer hardly spreads to the end. Thus, when it is difficult for the polymer to spread to the end portion, the polymer tends to stay at the end portion, so that a polymer gel is easily generated. In addition, since the polymer flow rate becomes slow at the upper part of the polymer channel wall surface, air tends to remain, and yarn breakage due to bubbles of the remaining air tends to occur.

  The present invention can be used in spinning of synthetic fibers and the like.

1 is a cross-sectional view parallel to polymer flow illustrating one embodiment of a rectangular spin pack of the present invention. It is a three-view figure explaining the shape of the wall surface of the upper pack case in this invention. It is sectional drawing parallel to the polymer flow of a round spinning pack. It is sectional drawing explaining the shape of the wall surface of the upper pack case in a round spinning pack. It is sectional drawing parallel to the polymer flow of the conventional rectangular spinning pack. It is a three-plane figure explaining the shape of the wall surface of the upper pack case in the conventional rectangular spinning pack. It is a three-view figure explaining the shape of the wall surface of the upper pack case in one Embodiment of this invention. It is a three-view figure explaining the shape of the wall surface of the upper pack case in one Embodiment of this invention. It is a three-view figure explaining the shape of the wall surface of the upper pack case in one Embodiment of this invention. FIG. 7 is a diagram in which a virtual wall surface having a vertex at the value + 15% of Expression (1) and a virtual wall surface having a vertex at the value −15% of Expression (1) are added. FIG. 7 is a diagram in which a virtual wall surface having a vertex at the value + 20% of Expression (1) and a virtual wall surface having a vertex at the value −20% of Expression (1) are added. It is a numerical analysis result of the polymer flow velocity distribution in the upper pack case which has a polymer flow path shown in FIG. It is a numerical analysis result of the polymer flow velocity distribution in the upper pack case having the polymer flow path shown in FIG. FIG. 11 is a numerical analysis result of a polymer flow velocity distribution in an upper pack case having a polymer flow channel set to a value of + 15% of the value of equation (1) shown in FIG. 10. FIG. 11 is a numerical analysis result of a polymer flow velocity distribution in an upper pack case having a polymer flow channel set to a value of −15% of the value of equation (1) shown in FIG. 10. It is a numerical analysis result of the polymer flow velocity distribution in the upper pack case which has the conventional polymer flow path shown in FIG. It is a numerical analysis result of the polymer flow velocity distribution in the upper pack case where the polymer flow path wall surface shown in FIG. FIG. 10 is a numerical analysis result of a polymer flow velocity distribution in the upper pack case where the polymer flow path wall surface shown in FIG. 12 is a numerical analysis result of a polymer flow velocity distribution in an upper pack case having a polymer flow channel set to a value of + 20% of the value of the equation (1) shown in FIG. 12 is a numerical analysis result of a polymer flow velocity distribution in an upper pack case having a polymer flow path set to a value of −20% of the value of the expression (1) shown in FIG. 11. It is a three-view figure explaining the shape of the wall surface of the upper pack case at the time of applying patent document 1 to a rectangular spinning pack.

Explanation of symbols

1: Upper pack case 2: Filter material 3: Perforated plate 4: Base 5: Lower pack case 6: Polymer inflow pipe 7: Packing 8: Tightening bolt F ₁ : Polymer flow path

Claims (4)

In the lower pack case, a filter medium, a perforated plate, and a base having a rectangular hole arrangement as viewed from above are arranged in this order in the direction of the entire flow of the polymer to be spun. A spinning pack in which a plate and a base are integrally assembled with an upper pack case, and the upper pack case has a polymer flow path whose cross-sectional shape is rectangular when viewed in a cross section orthogonal to the entire polymer flow. A rectangular spinning pack characterized in that when viewed in a cross section passing through the central axis of the spinning pack and parallel to the flow of the entire polymer, the slope of the wall surface of the polymer flow channel becomes gradually divergent as it goes downstream. In the polymer flow path, the center axis of the spin pack is the z-axis with the polymer flow direction being negative, the point where the z-axis and the upper pack case outflow surface intersect is the origin, and passes through the origin to be parallel to one side of the upper pack case outflow surface. X axis, the direction passing through the origin and perpendicular to the x axis is y axis, the distance from the upper pack case outflow surface to the polymer inflow pipe outflow surface is L, and the polymer inflow pipe radius is r, perpendicular to the z axis The cross section of the polymer flow path is

The rectangular spinning pack according to claim 1, wherein the rectangular spinning pack is a rectangle having a vertex satisfying the above and having a vertex within a range of ± 15%.
Where X ₁ is ½ of the length of one side in the x-axis direction on the outflow surface of the upper pack case
Y ₁ : 1/2 of one side length in the y-axis direction on the outflow surface of the upper pack case In the polymer flow path, the center axis of the spin pack is the z-axis with the polymer flow direction being negative, the point where the z-axis and the upper pack case outflow surface intersect is the origin, and passes through the origin to be parallel to one side of the upper pack case outflow surface. X axis, the direction passing through the origin and perpendicular to the x axis is the y axis, the distance from the upper pack case outflow surface to the polymer inflow pipe outflow surface is L, the polymer inflow pipe radius is r, the polymer flow path is dividing the z = 0 to n _max stage in the z-axis direction as a first stage, a polymer flow path cross section perpendicular to the n-th stage of the z-axis is z = z _n is represented by the following formula (1)

It has a rectangle having an apex at the central value and to the range of ± 15% of the points which satisfy the the respective sides of a rectangular n-th cross-section that the polymer flow path wall at _{z = z n, z = z} n + 1 The rectangular spinning pack according to claim 1, wherein each of the rectangular sides of the (n + 1) -th stage cross section is a plane connected by a straight line.
Where X ₁ is ½ of the length of one side in the x-axis direction on the outflow surface of the upper pack case
Y ₁ : 1/2 of one side length in the y-axis direction on the outflow surface of the upper pack case A synthetic fiber spinning method comprising spinning using the rectangular spinning pack according to any one of claims 1 to 3.

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