• 专利附录
  • 专利说明
  • 权利要求
  • 类似技术
  • 同族专利
  • 引用文献
  • 法律状态
  • 优先权
    • 专利摘要:
    A pipe molding die of the present invention is capable of rectifying a flow of a molten resin by a resin reservoir and uniformizing the flow of the resin extruded from the die in whichever position in a peripheral direction on a flow path within the die. Consequently, ununiformity in wall thickness of the resin pipe to be molded can be eliminated. The pipe molding die comprises a throttle part as one of components thereof, which includes a core, a shell part fitted to the core and a resin reservoir as a portion of a flow path which is formed between the core and the shell part. A molten resin as a pipe raw material flows through the flow path. The resin reservoir is provided in at least one of the core and the shell part, and takes a ring-like shape circumscribing a central axis of the pipe molding die with the central axis centered. The resin reservoir assumes a recessed shape in cross-section.
    公开号:US20010001672A1
    申请号:US08/952,476
    申请日:1997-03-13
    公开日:2001-05-24
    发明作者:Yoshihiro Yoshimura；Katunari Nishimura；Takumi Murata；Masahiro Yamada
    申请人:Mitsui Chemicals Inc；
    IPC主号:B29C48-705
    专利说明:
    [0001] The present invention relates to a pipe molding die and a resin pipe molded by the pipe molding die. [0001] BACKGROUND ART
    [0002] A pipe molding die is employed for manufacturing an elongate resin pipe such as a polypropylene pipe and a polyethylene pipe that are used as, e.g., gas pipes. [0002]
    [0003] The pipe molding die is supplied, from a resin extruder, with a molten kneaded resin (The molten kneaded resin will hereinafter be termed a “molten resin”.) defined as a raw material for the resin pipe. The supplied molten resin is discharged finally in the form of a resin pipe as an extrusion molded product from the die via a flow path within the die. According to procedures thereof, the molten resin supplied into the die is temporarily expanded in a cylindrical shape, and thereafter gradually throttled down into a pipe in the end that has a diameter corresponding to an application. [0003]
    [0004] In general, the pipe molding die is basically constructed of a die part, a throttle part and a land part. The die part forms the molten resin supplied in from a resin extruder in a cylindrical shape. The throttle part gives a rectifying effect by throttling the cylindrical molten resin fed in from the die part. And the land part uniforms a flow velocity of the resin. Then, those constructive parts are each concentrically arranged in sequence from an upstream side to a downstream side in a flowing direction of the molten resin. [0004]
    [0005] The resin pipe as an extrusion molded product manufactured by the pipe molding die described above is required to have no ununiformity in terms of wall thickness. Namely, it is required that both of an inner surface configuration and an outer surface configuration of the resin pipe be concentrically complete rounds as viewed in cross-section. [0005]
    [0006] It is because problems as shown in the following items (1)-(3) might arise if the pipe has the ununiformity in wall thickness. [0006]
    [0007] (1) It is undesirable in terms of external appearance. [0007]
    [0008] (2) A core deviation tends to occur when in a butt seam fusion to fuse end surfaces of the pipe by butting them with each other. [0008]
    [0009] (3) Contaminations and flaw on the surface of the pipe are undesirable for joining a joint to the pipe by fusion, and therefore the pipe surface is required to be cut. In that case, an outer peripheral surface of the pipe is fixed by a jig, and the pipe surface is cut by a cutting tool while moving the cutting tool along the pipe. If ununiformity in wall thickness is large, however, the pipe can not be uniformly held by the jig because of the ruggedness on the pipe surface, with the result that there might be a firmly fixed portion and a slackened portion to make the pipe unstable. Further, since a distance between the outer surface of the pipe fixed by the jig and the cutting tool is not uniform, an adhesion is poor, and a complete round can not be obtained even when cut off. Besides, unevenness in cutting is to appear. A cutting quantity must increase in order to prevent the unevenness in cutting, and correspondingly a more extra of pipe raw material is needed. [0009]
    [0010] Such being the case, it is a general practice that a flow of the resin extruded from the die is kept constantly in whichever position on a flow path within the die to uniformize the wall thickness of the resin pipe to be molded by the pipe molding die. Methods of enhancing a rectifying effect and a throttle effect are effective in terms of keeping constantly the flow of the resin through the flow path. [0010]
    [0011] For making an attempt to enhance the rectifying effect and the throttle effect as well, the die must be increased in size. When increasing the size of the die, a pressure necessary for flowing the molten resin has to be risen. Furthermore, if the pressure rises, a temperature of the molten resin increases enough to easily deteriorate the resin or to cause an excessive luster on the pipe surface to such an extent as to be visually undesirable, resulting in a devaluation of a commercial product. Then, pressure tightness of the die and of the extruder must be increased. [0011]
    [0012] Moreover, according to the tests by the present inventors, it has proved that the ununiformity in wall thickness is to occur even when making an endeavor to enhance the rectifying effect and the throttle effect in the technologies contrived so far in the case of manufacturing a pipe that is equal to or larger than 8 mm in wall thickness. [0012]
    [0013] It is an object of the present invention to provide a pipe molding die capable of simply preventing an occurrence of ununiformity in wall thickness of a resin pipe irrespective of a degree of desired dimension of the wall thickness of the resin pipe, and also a resin pipe molded by this pipe molding die. [0013] DISCLOSURE OF INVENTION
    [0014] A pipe molding die according to the present invention comprises a throttle part defined as one of constructive parts thereof. This throttle part includes a core, a shell part fitted to the core, and a resin reservoir as a portion of a flow path. The flow path being formed between the core and the shell part. A molten resin as a pipe raw material flows through the flow path. [0014]
    [0015] The resin reservoir is provided in at least one of the core and the shell part and takes a ring-like shape circumscribing a central axis of the pipe molding die with the central axis centered. Further, the resin reservoir assumes a recessed shape in cross-section. [0015]
    [0016] The thus constructed pipe molding die according to the present invention, a flow of the resin extruded from the die can be uniformized in whichever position on the flow path within the die owing to the resin reservoir, and it is therefore feasible to restrain a momentum of the flow of the molten resin. Consequently, the flow becomes smooth to enhance a rectifying effect. Accordingly, no ununiformity in wall thickness of the resin pipe to be molded can be seen. [0016]
    [0017] Moreover, a capacity of the resin reservoir may be varied corresponding to a dimension of desired wall thickness of the molded resin pipe, i.e., the resin reservoir may be so formed as to decrease the capacity thereof in the case of a thin resin pipe but increase the capacity thereof in the case of a thick resin pipe. A quantity of the molten resin in a longitudinal direction (The longitudinal direction means from an upstream side to a downstream side of the flow path.) at the throttle part is thereby kept constant regardless of a degree of dimension of desired wall thickness of the resin pipe. The keeping constantly the quantity of the molten resion at the throttle part makes it possible to prevent an occurrence of the ununiformity in wall thickness of the resin pipe. [0017]
    [0018] Thus, a size of the resin reservoir provided in the throttle part as one of the constructive parts of the die, is simply set corresponding to the wall thickness of the resin pipe to be molded, whereby the rectifying effect can be enhanced without increasing the size of the die itself. [0018]
    [0019] The flow path described above may include a throttle taking a constricted shape narrower than other parts along this flow path, and this throttle may be formed with the resin reservoir described above. [0019]
    [0020] Moreover, it is desired that the resin reservoir be formed in such a configuration as not to cause a stagnation and a residence (The stagnation and the residence are hereinafter generically termed a “stagnation”.) in the flow of the molten resin. It is desirable that a recess cross section of the resin reservoir is formed for example in a curved-surface configuration, espacially is a semi-circular configuration. In that case, it is preferably that a radius of curvature be 10 mm-100 mm, and an angle made by the central axis and each of tangential lines at both ends of a semi-circular arc of the resin reservoir be 15°-120°. [0020]
    [0021] Further, it is more desirable that the radius of curvature be 25 mm, and the angle be 75°-90°. [0021]
    [0022] The resin pipe according to the present invention is molded by using the pipe molding die as well as being molded of polyolefine as a pipe raw material. [0022]
    [0023] Polyolefine as the pipe raw material is desirably polyethylene. [0023]
    [0024] Furthermore, it is preferable that the resin pipe be manufactured so that an average wall thickness thereof is set to one of values in a range of 5 mm-50 mm, and that a difference between a maximum wall thickness and a minimum wall thickness of the pipe is equal to or smaller than 1.0 mm and, preferably, equall to or smaller than 0.3 mm. [0024] BRIEF DESCRIPTION OF DRAWINGS
    [0025] FIG. 1 is a vertical sectional view of a pipe molding die according to the present invention; [0025]
    [0026] FIG. 2 is an enlarged view of the principal portion in FIG. 1; [0026]
    [0027] FIG. 3 is an enlarged view of the principal portion in FIG. 2; [0027]
    [0028] FIG. 4 is an example of variation of that shown in FIG. 2, in which a portion for forming a resin reservoir is different; [0028]
    [0029] FIG. 5 is another example of variation of that shown in FIG. 2, in which the portion for forming the resin reservoir is different; [0029]
    [0030] FIG. 6 is a view showing a comparative example with a resin reservoir according to the present invention; [0030]
    [0031] FIG. 7 is a view showing another comparative example with the resin reservoir according to the present invention; [0031]
    [0032] FIG. 8 is a diagram showing a distribution of wall thickness of a polyethylene pipe molded by a pipe molding die according to the present invention; [0032]
    [0033] FIG. 9 is a diagram of comparison with FIG. 8, showing a distribution of wall thickness of a polyethylene pipe molded by a prior art pipe molding die; and [0033]
    [0034] FIG. 10 is a view illustrating a hitherto-existing throttle portion having no resin reservoir, and corresponding to FIGS. 3, 6 and [0034] 7. BEST MODE OF CARRYING OUT THE INVENTION
    [0035] Preferred embodiments of the present invention will hereinafter be described with reference to the drawings. [0035]
    [0036] FIG. 1 is a vertical sectional view showing one example of a pipe molding die. [0036]
    [0037] In this pipe molding die [0037] 1, a molten resin is supplied from a left end in FIG. 1, and similarly a resin pipe P having a desired diameter as an extrusion molded product, is discharged from the right end. More specifically, the left end side of FIG. 1 corresponds to an upstream side in a flowing direction of a molten resin p, while the right end side of the same corresponds to a downstream side. Hereinbelow, the upstream and downstream sides in the flowing direction of the molten resin p are simply termed an “upstream side” and a “downstream side”.
    [0038] The die [0038] 1 is constructed roughly of three parts. Videlicet, they are a die part 2, a throttle part 3 and a land part 4. These parts are arranged in sequence from the upstream side to the downstream side of the molten resin p. Inside the individual parts 2, 3 and 4, consecutive flow paths which will be mentioned later on are provided respectively. Then, the molten resin p flows sequentially through those flow paths.
    [0039] The die part [0039] 2 is a part located on the upstream side of the die 1 and is a part for receiving the molten resin p supplied from an unillustrated resin extruder. The molten resin p supplied to the die part 2 passes through the die part 2 and arrives at the throttle part 3.
    [0040] Further, the die part [0040] 2 consists of a core 2 a and a shell part 2 b into which the core 2 a is inset.
    [0041] The core [0041] 2 a is located on a central axis L of the die 1 and is a cylindrical body, an upstream-side end portion of which is conically pointed. Note that the throttle part 3 and the land part 4 respectively have a core 3 a and a core 4 a, which are also located on the central axis L.
    [0042] The shell part [0042] 2 b, which takes a cylindrical shape on the whole with one end opened and the other end closed, includes a disk-like proximal seat member 2 b 1 located at an upstream-side end and an external cylindrical portion 2 b 2 occupying other portions of the shell part 2 b. The external cylindrical portion 2 b 2 is a hollow cylindrical member extending from a peripheral edge of the proximal seat member 2 b 1 toward the downstream side.
    [0043] Further, the proximal seat member [0043] 2 b 1 has such a flat recessed portion as being hollowed out in a conical shape at the center thereof enough to receive the above upstream side end of the core 2 a, and the external cylindrical portion 2 b 2 covers the cylindrical portion of the core 2 a.
    [0044] A flow path [0044] 2 c and a flow path 2 d of the die part 2 are respectively formed between the core 2 a and the proximal seat member 2 b 1 and between the core 2 a and the external cylindrical portion 2 b 2.
    [0045] The flow path [0045] 2 c looks like a generally trigonal pyramid shape as the whole (The flow path 2 c appears a forked shape gradually expanding as it approaches the downstream side in FIG. 1.). Then, an apex side of the flow path 2 c, which is located on the upstream side, is opened. Note that the aperture of the flow path 2 c serves as a molten resin receiving port for receiving the molten resin into the pipe molding die 1 from the resin extruder, and is designated by the numeral 7.
    [0046] The flow path [0046] 2 d is continued with the right side of the flow path 2 c, and takes a cylindrical configuration on the whole (In FIG. 1 the flow path 2 d appears to be two lines of parallel passageways continuous from the forked flow path 2 c.). A diameter of the flow path 2 d is larger than a diameter of the resin pipe P, and a screw groove 8 is formed in an internal peripheral portion of the flow path 2 d.
    [0047] The molten resin p entering the flow path [0047] 2 d from the flow path 2 c goes on flowing toward the throttle part 3 while changing its flowing shape into a cylindrical shape from a triangular conical shape as the flow thereof advances.
    [0048] Note that the die part [0048] 2 has the screw groove 8 as stated above, and hence the die 1 is termed a spiral die. The die is classified, in addition to this, into a spider die, a cross head die, a basket die and other types of dies. In the great majority of cases, the spiral die is used, however, the variety of dies are separately employed according to the applications and necessities.
    [0049] The throttle part [0049] 3 is a part located between the die part 2 and the land part 4, and is a part for giving a so-called rectifying effect. More specifically, as already mentioned, the throttle part 3 is a part which admits a passage of the molten resin p flowing in from the flow path 2 d in the cylindrical shape on the whole while being temporarily expanded larger in terms of its diameter than the resin pipe P, and gradually throttles the diameter of the cylindrical molten resin p down to the diameter of the resin pipe P.
    [0050] The throttle part [0050] 3 described above is constructed of a core 3 a and a shell part 3 b fitted to an outer portion of the core 3 a.
    [0051] The core [0051] 3 a comprises a head-cut conical part 3 a 1 and a cylindrical part 3 a 2. The head-cut conical part 3 a 1 occupies a half on the upstream side and taking a head-cut conical shape, and a cylindrical part 3 a 2 similarly occupies a half on the downstream side and taking a cylindrical shape.
    [0052] The shell part [0052] 3 b has a fitting seat member 3 b 1 and a throttle element 3 b 2. The fitting seat member 3 b 1 corresponds to the head-cut conical part 3 a 1 of the core 3 a, and the throttle element 3 b 2 corresponds to the cylindrical part 3 a 2 of the core 3 a, respectively.
    [0053] The fitting seat member [0053] 3 b 1 assumes a channel-like configuration in cross-section, and a side wall part 3 b 1-1 located on the upstream side thereof is formed with a hole 3 b 1-2, into which the head-cut conical part 3 a 1 is inserted, taking the same configuration as this. Further, the cylindrical part 3 a 2 of the core 3 a is located on the central axis L in a space 10 surrounded by a peripheral wall part 3 b 1-3 of the fitting seat member 3 b 1. Then, the ring-like throttle element 3 b 2 is fitted to an outer periphery of this cylindrical part 3 a 2.
    [0054] When the core [0054] 3 a and the throttle element 3 b 2 are fitted to the fitting seat member 3 b 1, a flow path 3 c is formed between the hole 3 b 1-2 of the side wall part 3 b 1-1 of the fitting seat member 3 b 1 and the head-cut conical part 3 a 1 of the core 3 a, and a flow path 3 d is formed between the throttle element 3 b 2 and the cylindrical part 3 a 2 of the core 3 a.
    [0055] The flow path [0055] 3 c which is a flow path is continued with the right side of the flow path 2 d of the die part 2 and formed a head-cut conical shape on the whole, and the head-cut side thereof is directed toward the downstream side (The flow path 3 c appears to be two lines of passageways narrowing down on the downstream side in FIG. 1.).
    [0056] The flow path [0056] 3 d is continued with the right side of the flow path 3 c and assumes the cylindrical shape on the whole. Further, the flow path 3 d is smaller in diameter than the flow path 2 d similarly taking the cylindrical shape in the die part 2 (The flow path 3 d appears two lines of parallel passageways continuous from the flow path 3 c in FIG. 1.). The flow path 3 d is wide both at the upstream end and at the downstream end thereof, but is constricted narrowly at the central portion. This constricted part is referred to as a throttle designated by the numeral 11. The throttle 11 is formed in such a manner that the central part of an inner peripheral surface 3 b 2-1 of the throttle element 3 b 2 is protruded in a trapezoidal shape on the side of the central axis L.
    [0057] The throttle [0057] 11 is, as obvious from FIG. 3, provided with a resin reservoir 13 serving as a portion of the flow path 3 d at the central portion thereof. The resin reservoir 13, which is a recessed portion provided in the throttle 11 and opened on the side of the central axis L, takes a ring-1ike shape about the central axis L. Further, the resin reservoir 13, as obvious from FIGS. 2 and 3, is semi-circular in cross-section and is 25 mm in curvature radius R. The curvature radius R is not, however, limited to 25 mm and, though an acceptable range may be 10 mm-100 mm, desirably falls within a range of preferably 10 mm-50 mm in terms of enhancing the rectifying effect and preventing so-called black burning by decreasing a residence time of the molten resin within the resin reservoir 13.
    [0058] Set, also as shown in FIG. 3, within a range of 75-90° is an angle α made by a tangential line t drawn at the upstream-side end [0058] 13 a and at the downstream-side end 13 b of the resin reservoir 13 (Only one tangential line drawn at the upstream-side end 13 a is shown.), in other words, drawn at the two ends 13 a, 13 b of a semi-circular arc 13 c in cross-section of the resin reservoir 13, and by the central axis L (in other words, a wall surface 3 a 2′ of the cylindrical part 3 a 2 parallel to the central axis L). The angle α is not, however, confined to the range of 75-90° and may fall within a range of 15-120°. In short, this range may be the one enough to enhance the rectifying effect by the resin reservoir 13, not to cause a stagnation and to prevent the black-burning, and preferably the one of 75-90° in terms of the effect. The numerical values given above are calculated based on an endorsement through the tests implemented by the present inventors.
    [0059] Note that the angle α is shown in the Figures in the two cases of its being made by the tangential line t and the central axis L, and by the tangential line t and the wall surface [0059] 3 a 2′ of the cylindrical part 3 a 2 parallel to the central axis L.
    [0060] Moreover, the two ends [0060] 13 a, 13 b of the circular arc are so formed as to be curvilinearly bent enough not to hinder a small influx of the molten resin. Then, gaps “a”, “b” between the two ends 13 a, 13 b and the cylindrical part 3 a 2 are set to 2 mm. The gaps are not, however, limited to 2 mm and are, though an acceptable range may be 0.5 mm-5 mm, desirably set to a range of preferably 1 mm-3 mm.
    [0061] Then, the resin reservoir [0061] 13 is not provided in the fitting seat member 3 b 1 but may be, as illustrated in FIG. 4, provided in the cylindrical part 3 a 2 of the core 3 a. Further, as shown in FIG. 5, the resin reservoir 13 may be provided in both of those parts.
    [0062] Moreover, the throttle [0062] 11 formed with the resin reservoir 13 may be provided at the cylindrical part 3 a 2 of the core 3 a and may be provided both at the throttle element 3 b 2 and at the cylindrical part 3 a 2.
    [0063] Further, the cross-sectional shape of the resin reservoir [0063] 13 may be, in addition to the semi-circular shape, shapes of smoothly curved surfaces such as circular arcs in other forms, a part of elliptical shape parabolic shape and so forth causing no stagnation of the flow of the molten resin p. However, the semicircular shape in cross section is the best in terms of causing no stagnation of the flow of the molten resin, and is easy to work.
    [0064] The resin reservoir [0064] 13 may be formed in other places than the throttle 11 in the flow path 3 d.
    [0065] Note that FIGS. 6 and 7 show a comparative examples with the resin reservoir [0065] 13 according to the present invention. If the resin reservoir 13 takes a rectangular shape in cross-section with corners rounded as illustrated in FIG. 6 or an isosceles triangular shape in cross-section with an apex rounded as shown in FIG. 7, it might happen that the molten resin is stagnated at the corners and the apex thereof. As the result, the resin is burned black and the burned substances are adhered to the corners and the apex as well. Accordingly, it is of importance how the configuration of the resin reservoir 13 is selected.
    [0066] The land part [0066] 4 is a part, located on the downstream side of the die 1, for uniformizing a flow velocity of the molten resin.
    [0067] Such land part [0067] 4 is constructed of a core 4 a and a shell part 4 b fitted to an outer portion of the core 4 a.
    [0068] The core [0068] 4 a has a configuration similar to the core 3 a of the throttle part 3, and is constructed of a head-cut conical part 4 a 1 corresponding to the head-cut conical part 3 a 1 and a cylindrical part 4 a 2 corresponding to the cylindrical part 3 a 2 of the core 3 a. The head-cut conical part 4 a 1 is, however, by far smaller in difference between the upstream side and the downstream side than in the head-cut conical part 3 a 1. Further, the head-cut conical part 4 a 1 is hollow.
    [0069] The shell part [0069] 4 b includes a flange member and takes a cylindrical shape on the whole. The shell part 4 b comprises a flange part 4 b 1 having the same major diameter as that of the throttle element 3 b 2 of the core 3 a and being contiguous to the throttle element 3 b 2, and an outer cylindrical part 4 b 2 extending from a portion, closer to the central axis L, of the flange part 4 b 1 toward the downstream side.
    [0070] A flow path [0070] 4 c and a flow path 4 d of the land part 4 are respectively formed between the head-cut conical part 4 a, of the core 4 a and the flange part 4 b 1 of the outer shell part 4 b, and between the cylindrical part 4 a 2 of the core 4 a and the outer cylindrical part 4 b 2 of the outer shell part 4 b.
    [0071] The flow path [0071] 4 c is a flow path continuous on the right side of the flow path 3 d of the throttle part 3 and takes an extremely gently slant head-cut conical shape, and a head-cut side thereof is directed rightward in FIG. 1 (The flow path 4 c appears to be two lines of passageways in which a spacing therebetween is narrowed down extremely gently from the flow path 3 d of the throttle part 3 as it approaches toward the downstream side in FIG. 1.).
    [0072] The flow path [0072] 4 d is continued with the right side of the flow path 4 c and assumes a cylindrical configuration on the whole. The flow path 4 d is smaller in diameter than the flow path 3 d similarly taking the cylindrical shape (The flow path 4 d appears two lines of parallel passageways continuous from the flow path 4 c in FIG. 1, wherein a width dimension “w” of each of the passages appearing parallel is so set as to be a wall thickness of the resin pipe P defined as an extrusion molded product.). A diametrical dimension “W” of the flow path 4 d is, i.e., a diametrical dimension of the resin pipe P.
    [0073] Incidentally, what is indicated by the numeral [0073] 15 is an outlet of the flow path 4 d, in other words, a pipe discharge port of the die 1, from which the resin pipe P defined as the extrusion molded product is finally discharged.
    [0074] According to the thus constructed die [0074] 1, when the molten resin p from the resin extruder is supplied into the die 1 through a molten resin receiving port 7, this molten resin p is led inwardly of the die 1 along a route such as flow path 2 c→flow path 2 d→flow path 3 c→flow path 3 d→flow path 4 c→flow path 4 d, and thereafter discharged, in the form of the resin pipe P as the extrusion molded product, out of the pipe discharge port 15 of the die 1.
    [0075] FIG. 8 shows a distribution of wall thickness of a polyethylene pipe molded by the pipe molding die according to the present invention. It can be understood from FIG. 8 that a difference between a maximum wall thickness and a minimum wall thickness of the pipe, viz., an ununiformity in wall thickness is extremely equal to or smaller than 0.3 mm, and therefore a neat circle is depicted. [0075]
    [0076] Set conditions in this case are as follows: [0076]
    [0077] Curvature radius R=25 mm [0077]
    [0078] α=75-90° [0078]
    [0079] a, b=2 mm [0079]
    [0080] Nominal dimension=200 mm (major diameter: 216 mmφ, and average wall thickness: 17 mm). [0080]
    [0081] FIG. 9 is a diagram compared with FIG. 8, and shows a distribution of wall thickness of the polyethylene pipe molded by the pipe molding die in the prior art, wherein the polyethylene pipe having the same nominal dimension of 200 as the one described above is manufactured by the die with the throttle [0081] 11 including no resin reservoir 13 as shown in FIG. 10. As can be understood from FIG. 9, the difference between the maximum wall thickness and the minimum wall thickness of the pipe, i.e., the ununiformity in wall thickness is 1.6 mm, and ruggedness on a pipe surface (a pipe internal surface) can be seen.
    [0082] Thus, the die [0082] 1 according to the present invention includes the resin reservoir 13, whereby there could be obtained the polyethylene pipe with a remarkably reduced ununiformity in wall thickness, which pipe is substantially a complete round in cross-section. Note that the pipe is not confined to the polyethylene pipe using polyethylene as a pipe raw material but may embrace a polyolefine pipe using polyolefine as a pipe raw material. The die 1 according to the present invention is, however, optimal to the molding of the polyethylene pipe.
    [0083] As a result of generalizing the tests performed by the present inventors, the major diameter (diameter) and the average wall thickness of the resin pipe P formed by the pipe molding die [0083] 1 applied thereto are set respectively within a range of 60 mm-500 mm and a range of 5 mm-50 mm, however, it could be recognized that the resin pipe becomes preferable by setting the major diameter of the resin pipe P within a range of 80 mm-220 mm and the average wall thickness of the pipe P within a range of 8 mm-20 mm.
    [0084] Then, in the distribution of wall thickness of the resin pipe P, the wall thickness ununiformity conceived as the difference between the maximum wall thickness and the minimum wall thickness can be set within a range of 0 mm-1.0 mm in the normal setting described above and a range of 0 mm-0.3 mm in the preferable setting described above, and therefore it proved that the preferable resin pipe can be manufactured. [0084]
    [0085] When the resin pipe P is thus manufactured by use of the die [0085] 1 according to the present invention, the resin p extruded from the die 1 can be flowed uniformly in whichever position on the flow path 3 d within the die 1 owing to the resin reservoir 13, and it is therefore feasible to restrain a momentum of the flow of the molten resin p. Consequently, the flow of the molten resin p gets smooth enough to enhance the rectifying effect. Accordingly, it is possible to prevent the occurrence of the ununiformity in wall thickness of the resin pipe P to be molded, and also it is possible to obtain the resin pipe P with the minor and major diameters that are both substantially the complete rounds.
    [0086] Incidentally, it can be expected that the above effect is enhanced all the more in combination with the throttle effect. [0086]
    [0087] Further, the ununiformity in wall thickness can be reduced, and hence the problems described in the items (1)-(3) in the description of the prior art can be obviated. [0087] INDUSTRIAL APPLICABILITY
    [0088] As discussed above, in the pipe molding die according to the present invention, the flow of the molten resin is rectified by the resin reservoir, and the flow of the resin extruded from the die can be uniformed in whichever position in the peripheral direction on the flow path within the die. Therefore, the pipe molding die is applicable as the one capable of preventing the ununiformity in wall thickness of the resin pipe to be molded. Further, the resin pipe manufactured by using this pipe molding die has no ununiformity in wall thickness, and therefore a utility value thereof becomes higher correspondingly. [0088]
    权利要求:
    Claims (8)
    [1" id="US-20010001672-A1-CLM-00001] 1. A pipe molding die comprising:
    a throttle part defined as one of parts constituting said pipe molding die,
    said throttle part including:
    a core;
    a shell part, fitted to said core, for forming a flow path through which a molten resin as a pipe raw material flows between said core and said shell part; and
    a resin reservoir provided in at least one of said core and said shell part as a portion of said flow path and taking a recessed shape in cross-section and a ring-like shape circumscribing a central axis of said pipe molding die with this central axis centered.
    [2" id="US-20010001672-A1-CLM-00002] 2. The pipe molding die according to
    claim 1 , wherein said flow path has a throttle in a shape constricted thinner than other portions along said flow path, and said throttle is formed with said resin reservoir.
    [3" id="US-20010001672-A1-CLM-00003] 3. The pipe molding die according to
    claim 1 or
    2 , wherein a recessed cross section of said resin reservoir is formed in a curved-surface configuration to prevent a flow of the molten resin from being stagnated.
    [4" id="US-20010001672-A1-CLM-00004] 4. The pipe molding die according to any one of claims 1 through 3, wherein said resin reservoir is sem-icircular in cross-section, a radius of curvature thereof is 10 mm-100 mm, and an angle made by each of tangential lines at both ends of the semi-circular arc of said resin reservoir and by the central axis is 15-120°.
    [5" id="US-20010001672-A1-CLM-00005] 5. The pipe molding die according to
    claim 4 , wherein the radius of curvature is 25 mm, and the angle is 75°-90°.
    [6" id="US-20010001672-A1-CLM-00006] 6. The pipe molding die according to any one of claims 1-5, wherein said die is used for molding a polyolefine pipe involving the use of polyolefine as a pipe raw material.
    [7" id="US-20010001672-A1-CLM-00007] 7. The pipe molding die according to
    claim 6 , wherein the polyolefine is polyethylene.
    [8" id="US-20010001672-A1-CLM-00008] 8. A resin pipe characterized in that an average wall thickness of said pipe is set to one of values in a range of 5 mm-50 mm, that a difference between a maximum wall thickness and a minimum wall thickness of said pipe is equal to or larger than 0 mm but equal to or smaller than 1.0 mm, and said pipe is manufactured by said pipe molding die according to any one of claims 1 through 7.
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    同族专利:
    公开号 | 公开日
    CN1312155A|2001-09-12|
    WO1997035704A1|1997-10-02|
    KR19990014860A|1999-02-25|
    CN1193296A|1998-09-16|
    EP0834385B1|2003-08-20|
    TW346435B|1998-12-01|
    EP0834385A1|1998-04-08|
    EP0834385A4|1999-04-14|
    DE69724210D1|2003-09-25|
    US6338622B2|2002-01-15|
    CA2220977A1|1997-10-02|
    DE69724210T2|2004-06-17|
    CN1077841C|2002-01-16|
    JP3202024B2|2001-08-27|
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    DE2610972C2|1976-03-16|1984-04-12|Erich 7326 Heiningen Oprach|Device for the production of pipes or similar hollow strands made of thermoplastic material|
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    JPH04135731A|1990-09-27|1992-05-11|Mitsubishi Plastics Ind Ltd|Manufacture of thermoplastic resin pipe|
    FR2710286B1|1993-09-22|1995-12-08|Plastic Omnium Cie|Hollow body in fluorinated resin, process for its manufacture and extrusion press for the implementation of the process.|US6665307B1|1999-07-02|2003-12-16|Telefonaktiebolaget Lm Ericsson |Variable fast page mode|
    KR100315760B1|1999-10-18|2001-12-12|변무원|An Apparatus for Forming a Corrugated Pipe|
    AT414317B|2004-11-15|2007-02-15|Greiner Extrusionstechnik Gmbh|MOLDING DEVICE AND METHOD FOR FORMING AND COOLING HOLLOW PROFILES|
    WO2006060345A2|2004-11-30|2006-06-08|Blackett Peter W|Extrusion die for the production of polymeric blown films|
    CN102275288A|2011-08-03|2011-12-14|句容市后白镇民生塑胶厂|Mould for producing plastic pipe|
    JP2020163623A|2019-03-28|2020-10-08|住友重機械工業株式会社|Inflation molding device|
    法律状态:
    1998-02-13| AS| Assignment|Owner name: MITSUI CHEMICALS, INC., JAPAN Free format text: ASSIGNMENT OF ASSIGNORS INTEREST;ASSIGNORS:YOSHIMURA, YOSHIHIRO;NISHIMURA, KATUNARI;MURATA, TAKUMI;AND OTHERS;REEL/FRAME:008979/0369 Effective date: 19971215 |
    2001-12-28| STCF| Information on status: patent grant|Free format text: PATENTED CASE |
    2005-06-21| FPAY| Fee payment|Year of fee payment: 4 |
    2008-09-03| AS| Assignment|Owner name: MITSUI CHEMICALS INDUSTRIAL PRODUCTS, LTD., JAPAN Free format text: ASSIGNMENT OF ASSIGNORS INTEREST;ASSIGNOR:MITSUI CHEMICALS, INC.;REEL/FRAME:021462/0857 Effective date: 20080528 |
    2009-06-17| FPAY| Fee payment|Year of fee payment: 8 |
    2013-03-11| FPAY| Fee payment|Year of fee payment: 12 |
    优先权:
    申请号 | 申请日 | 专利标题
    JP8-067750||1996-03-25||
    JP6775096||1996-03-25||
    PCT/JP1997/000805|WO1997035704A1|1996-03-25|1997-03-13|Pipe extrusion die and resin pipe|
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