JP2006103139A - Cylinder hopper - Google Patents

Abstract

<P>PROBLEM TO BE SOLVED: To improve the treatment capacity of a screw type kneading extruder that melts and kneads a crushed product of films. <P>SOLUTION: In a cylinder hopper which supplies, into the cylinder inner hole of a twin screw kneading extruder having a cylinder in which a cylinder inner hole holding two screws in parallel and rotatably is formed, the film crushed product formed by crushing resin films as a raw material, through a communicating orifice communicating with the cylinder inner hole and an opening portion, a downstream side stepped portion 20b having an undercut 7 formed in its lower part is formed in such a manner as projected to the communicating orifice 20D, and a raw material supplying portion 4, wherein a raw material supplying port 9 is formed, is fitted inside the communicating orifice 20D so that the lower end part 4c<SB>1</SB>of the downstream side wall 4c of the raw material supplying portion 4 and the top part 20 b<SB>1</SB>of the downstream side stepped portion 20b may coincide. <P>COPYRIGHT: (C)2006,JPO&NCIPI

Description

  The present invention relates to a cylinder hopper that stably supplies a pulverized film to a twin-screw extruder. In the present invention, the “upstream side” refers to the raw material supply side of the twin screw extruder, and the “downstream side” refers to the side from which the manufactured molten resin is discharged.

  In general, as a method for regenerating defective products and product residue generated during plastic molding, or recovered products, a process of melting and kneading using a screw-type kneading extruder is performed. In the case of a regeneration process using a screw-type kneading extruder, plastics are crushed and then supplied as a pulverized raw material.

  When the plastic is a film, the pulverized raw material is generally irregular in shape and is not constant, and a large space is formed between the pulverized pieces of the raw material to contain a large amount of air, so that the bulk density is 0.02 g / cc to 0. Very small, 2 g / cc. If such a pulverized raw material is supplied as it is to the screw-type kneading extruder, a bridging phenomenon occurs in the raw material supply device, the bite into the screw is poor, the operation becomes unstable, and the processing efficiency becomes very low.

  In order to eliminate the bridging phenomenon of such a pulverized raw material having a small bulk density and an uneven shape and to improve the biting property, a cylinder hopper as shown in FIGS. 3 and 4 has been proposed in a twin screw extruder. .

  FIG. 3A is a schematic view showing the configuration of a conventional twin screw extruder, FIG. 3B is a side sectional view of a cylinder hopper, and FIG. 3C is FIG. 3B. It is an arrow sectional view of the AA direction shown in FIG.

  The twin screw extruder 100 includes a hopper 101 for supplying raw materials such as a pulverized film, a cylinder 102 in which a screw 121 is rotatably housed, and a cylinder for supplying the raw material supplied from the hopper 101 into the cylinder 102. It has a hopper 150, a chute 103 that supplies raw material from the hopper 101 to the cylinder hopper 150, and a screw driving device 104 that rotationally drives a screw 121 in the cylinder 102.

  As shown in FIGS. 3B and 3C, the cylinder hopper 150 is formed with a cylinder inner hole 122 into which the screw 121 is inserted, and a raw material supply communicating with the cylinder inner hole 122 is formed at the upper portion of the cylinder hopper. A mouth 123 is formed.

  As shown in FIG. 3B, an undercut 127 is formed in the lower portion of the downstream side wall 150 c of the cylinder hopper 150 from the downstream inner wall surface 125 of the raw material supply port 123 toward the downstream side. An opening 129 is formed from the upstream inner wall surface 128 of the raw material supply port 123 to the end position of the undercut 127. In this conventional example, the opening dimension ratio of the raw material supply port 123 indicated by the dimension 1 in the transport direction of the raw material and the outer diameter dimension D of the screw is 1 / D = 2.0. Moreover, the opening dimension ratio of the opening part 129 shown by the dimension L of the conveyance direction of a raw material and the outer diameter dimension D of a screw is L / D = 2.5. Further, as shown in FIG. 3C, a side cut 130 is formed in the vicinity of the cylinder inner hole 122 on the screw rotation side wall surface of the raw material supply port 123.

  The undercut 127 and the side cut 130 are for causing the supplied raw material to be wound into the screw 121 in a short time. The undercut 127 has a shape in which the cross-sectional area decreases toward the traveling direction so that the raw material can be smoothly bited in the traveling direction. The side cut 130 has a shape in which the opening area becomes smaller with respect to the rotation direction of the screw 121 so as to smoothly bite in the screw rotation direction.

  In the twin screw extruder 100 configured as described above, the film pulverized product as the raw material supplied from the hopper 101 to the chute 103 is forcibly supplied from the chute 103 into the cylinder 102 through the raw material supply port 123. Is done. In the cylinder 102, the raw material bites into the rotating screw 121 and is melt-kneaded while being transported in the downstream direction.

  FIG. 4 shows another conventional example of a cylinder hopper of a twin screw type extruder (see Patent Document 1).

  FIG. 4A is a schematic view showing the configuration of another conventional twin screw extruder, FIG. 4B is a side sectional view of the cylinder hopper, and FIG. 4C is FIG. It is arrow sectional drawing of the BB direction shown to (b).

  As shown in FIG. 4B, the cylinder hopper 250 is formed with a cylinder inner hole 232 into which the screw 231 is inserted, and a raw material supply port 239 communicating with the cylinder inner hole 232 is formed at the upper part of the cylinder hopper 250. A formed raw material supply unit 234 is attached.

  In the raw material supply unit 234, a void 236 is formed above the cylinder inner hole 232 from the downstream inner wall surface 235 of the raw material supply port 239 toward the downstream side, and on the downstream side of the void 236, An undercut 237 is formed to improve the biting characteristics of the raw material. The space 236 is a space surrounded by the wall surface 236 a parallel to the rotation axis of the screw 231 and the screw 231, and is a space surrounded by the undercut surface 237 a formed by the undercut 237 and the screw 231. Is not included. In the raw material supply unit 234, the opening 233 extends from the upstream inner wall surface 238 of the raw material supply port 239 to the tip of the undercut 237.

  In this conventional example, the opening size ratio of the raw material supply port 223 is 1 / D = 3.0, and the opening size ratio of the opening 229 is L / D = 2. It is set within the range of 5 to 8.0, and L / D = 4.7 in this example. Further, as shown in FIG. 4C, a side cut 240 is formed in the vicinity of the cylinder inner hole 232 on the screw rotating side wall surface of the opening 233 in the same manner as the cylinder hopper 150 shown in FIG.

In the cylinder hopper 250 shown in FIG. 4B, the L / D of the opening 233 is made particularly large with respect to the cylinder hopper 150 shown in FIG. ing.
JP 2002-307525 A

  However, in the case of the cylinder hopper 250 shown in FIG. 4 (b), although the L / D of the opening 233 is increased, the 1 / D of the raw material supply port 239 is not so expanded, and therefore the downstream. A space 236 is formed between the side inner wall surface 235 and the start position of the undercut 237. That is, since the opening area of the raw material supply port 239 is reduced by the amount of the empty space 236, when a film pulverized product having a small bulk specific gravity is used as the raw material, the biting ability is reduced. Moreover, since the angle between the rotating shaft of the screw 231 and the undercut surface 237a is formed at α = 15 ° to 30 °, the amount of biting is limited.

  In order to compensate for the decrease in the processing amount, if the screw rotation speed is increased to cope with it, the raw material may turn yellow due to the temperature rise of the raw material, so that it cannot be dealt with simply by increasing the rotational speed.

  In addition, if the rotational speed of the screw is lowered in order to avoid yellowing of the raw material, in the case of a film pulverized product having a small bulk specific gravity, a feed neck phenomenon that is pushed back to the supplied side tends to occur.

  As described above, in the processing of a pulverized film product having a small bulk specific gravity, there has been a problem that the operating range of the rotational speed of the twin screw type extruder becomes narrow.

  Furthermore, when a film pulverized product obtained by pulverizing a thin film is used as a raw material, the shape of the film pulverized product is thin and non-uniform in size. When received, the raw material was softened by the heat, and in the absence of the screw 231, the material was attached and softened to the raw material supply unit 234, which hindered supply.

  In order to solve the above problems, if the raw material supply member 234 is not used, the L / D of the raw material supply port 239 can be increased, but since the undercut 237 is eliminated, the raw material cannot be bitten smoothly, Eventually, the biting ability will be reduced.

  Then, an object of this invention is to provide the cylinder hopper which can improve the processing capability of the screw-type kneading extruder which melt-kneads a film ground product.

  In order to achieve the above object, the cylinder hopper of the present invention has a cylinder inner hole of a twin screw kneading extruder having a cylinder inner hole in which two screws are accommodated in parallel and rotatably. In the cylinder hopper that feeds the pulverized film formed by pulverizing the resin film as a raw material through the communication port and the opening communicating with the cylinder bore, the downstream stepped portion with the undercut formed in the lower portion communicates Protruding into the mouth, the raw material supply part where the raw material supply port is formed is installed in the communication opening so that the lower end of the downstream side wall of the raw material supply part and the top of the downstream stepped part are aligned. It is characterized by being.

  As described above, in the cylinder hopper of the present invention, the raw material supply unit is mounted in the communication port so that the lower end portion of the downstream side wall of the raw material supply unit and the top portion of the downstream stepped portion are matched. In other words, the raw material supply unit expands the raw material supply port to the top of the downstream side step portion so that a void formed in the past between the raw material supply unit and the cylinder bore is not formed. ing. Thereby, even if it is a case where the pulverized film product with a small bulk specific gravity is used as a raw material, it can prevent that a biting ability will reduce.

  Thus, since the cylinder hopper of the present invention can satisfactorily feed the raw material, the processing capacity of the raw material can be improved without increasing the rotational speed of the screw. In addition, since the raw material is melted and kneaded by a screw rotating at a low speed, yellowing of the resin due to an increase in the resin temperature can be prevented. Furthermore, since the cylinder hopper of the present invention can achieve good biting, it is difficult to generate a feed neck even when the screw is operated at a low speed.

  In the cylinder hopper of the present invention, when the dimension of the raw material in the transport direction is l and the outer diameter dimension of the screw is D, the opening dimension ratio of the raw material supply port is in the range of 1 / D = 4.0 to 9.5. It is more preferable to set it to be inside. If 1 / D is 4.0 or less, the biting ability is reduced, and if it is 9.5 or more, it is necessary to increase the overall length of the screw, and there is a risk of screw runout. Moreover, it is because the problem of a cost increase will also arise.

  Further, the cylinder hopper of the present invention may be one in which a flow path for flowing a refrigerant is formed in a wall that forms the outer periphery of the raw material supply port of the raw material supply unit. In this case, the pulverized film in contact with the wall surface of the raw material supply unit is not softened. Accordingly, it is possible to suppress a substantial decrease in the opening area due to the adhesion of the softened film pulverized product to the raw material supply port, which has conventionally hindered the raw material supply from the chute.

  Further, in the cylinder hopper of the present invention, if the angle β between the undercut surface facing the cylinder bore in the downstream stepped portion and the rotation shaft of the screw is 15 ° or less, the material bite is limited. If it is larger than 50 °, it becomes a mere wall and the raw material cannot be eaten, so that it is preferably larger than 15 ° and not more than 50 °.

  According to the cylinder hopper of the present invention, even when a film pulverized product having a small bulk specific gravity is used as a raw material, the raw material can be satisfactorily bitten. That is, the processing capability of the screw-type kneading extruder for melting and kneading the pulverized film can be improved by improving the raw material supply capability by the cylinder hopper of the present invention.

  Next, embodiments of the present invention will be described with reference to the drawings.

  The block diagram of the twin-screw type extruder of this embodiment is shown in FIG. Moreover, the schematic diagram of the cylinder hopper applied to the twin-screw type extruder of this embodiment in FIG. 2 is shown. 2A is a side cross-sectional view of an example of a cylinder hopper, FIG. 2B is a cross-sectional view in the direction of the CC shown in FIG. 2A, and FIG. 2C is a cylinder hopper. FIG. In addition, the screw 1 is abbreviate | omitted in FIG.2 (c).

  In the following description, the “upstream side” refers to the raw material supply side (left side in FIGS. 1, 2 (a), and 2 (c)) of the twin-screw extruder 50, and the “downstream side” "Refers to the side from which the manufactured molten resin is discharged (the right side in FIGS. 1, 2A, and 2C).

  A twin screw extruder 50 includes a hopper 51 that supplies raw materials such as a pulverized film formed by pulverizing a resin film, and a cylinder 52 in which two parallelly arranged screws 1 are rotatably accommodated. A cylinder hopper 20 that supplies the raw material supplied from the hopper 51 into the cylinder 52, a chute 53 that supplies the raw material from the hopper 51 to the cylinder hopper 20, and a screw drive device that rotationally drives the screw 1 in the cylinder 52 55.

As shown in FIGS. 2A and 2B, the cylinder hopper 20 is formed with a cylinder inner hole 2 in which two screws 1 arranged in parallel are rotatably accommodated. In addition, a communication port 20D for communicating the chute 53 and the cylinder inner hole 2 is formed in the upper portion of the cylinder inner hole 2, and a communication port is provided as a mounting portion 20c for mounting a raw material supply unit 4 described later. An upstream stepped portion 20a and a downstream stepped portion 20b projecting into 20D are provided. The lower part of the downstream step 20b is undercut, and this undercut 7 is formed. That is, the angle β between the undercut surface 7a facing the cylinder inner hole 2 and the rotation axis of the screw 1 is 15. It is formed within a range larger than 50 ° and 50 ° or smaller. This is because if the angle β is 15 ° or less, the biting of the raw material is restricted, and if it is larger than 50 °, it becomes a mere wall and the raw material cannot be bitten. Further, by performing an undercut process on the lower portion of the downstream side stepped portion 20b, the apex portion 20b ₁ that forms an acute corner between the undercut surface 7a and the surface with which the downstream side wall 4c of the raw material supply portion 4 abuts. Is formed.

  The raw material supply part 4 mounted on the mounting part 20c in the communication port 20D is formed with a rectangular raw material supply port 9 having the transport direction side surface 4a, the upstream side wall 4b, and the downstream side wall 4c as outer peripheral walls. The raw material supply unit 4 is positioned on the upper surface of the upstream stepped portion 20a and the downstream stepped portion 20b formed in the cylinder hopper 20, and is mounted on the mounting portion 20c.

The upstream side wall 4b of the raw material supply unit 4 is fitted along the side surface of the upstream side stepped portion 20a. The downstream side wall 4c of the raw material supply section 4, as the inner surface 4c ₂ of the downstream side wall 4c form a undercut surface 7a formed on the downstream side step 20b continuous surface, the lower end portion 4c ₁ of the downstream wall 4c Is matched with the top portion 20b ₁ of the downstream side step portion 20b. With such a configuration, even if the material supply unit 4 is mounted on the cylinder hopper 20, the void 236 as shown in the conventional example of FIG. 4B is not formed.

  The raw material supply port 9 indicates an opening that can be seen by the screw 1 when the cylinder hopper 20 is viewed from directly above, which is indicated by the dimension 1 in the raw material transport direction in FIG. The opening dimension ratio of the raw material supply port 9 is preferably 1 / D = 4.0 to 9.5, where D is the outer diameter dimension of the screw 1.

  In the present embodiment, the opening 3 refers to an opening having a dimension L in the raw material transport direction from the wall surface of the upstream side wall 4 b of the raw material supply unit 4 to the undercut 7.

  As a cooling mechanism for preventing a temperature rise due to heat transfer from the cylinder hopper 20 in the raw material supply unit 4, a flow path 16 formed substantially parallel to the raw material transport direction is formed in the transport direction side surface 4a. Yes. In each flow path 16 formed in each side surface 4a in the transport direction, a jacket inlet 14 through which cooling water as a refrigerant flows in and a jacket outlet 15 through which the water flows out are formed. In the case of the present embodiment, an example is shown in which the jacket inlet 14 and the jacket outlet 15 are provided so that the flow directions of the cooling water flowing in the flow paths 16 face each other, but the present invention is not limited to this. Absent. Moreover, as a refrigerant | coolant, not only cooling water but air, oil, and the fluid generally used as a refrigerant | coolant may be sufficient. Moreover, the flow path 16 may be formed not only in the transport direction side surface 4a but also in the upstream side wall 4b and the downstream side wall 4c. Further, these flow paths may be connected to each other to form a single flow path.

  Further, the flow rate and temperature of the cooling water supplied into the flow path 16 through the jacket inlet 14 are controlled by a control means 54 having a pump and a temperature control means (not shown). The temperature control means may have a heating part and a heat dissipation part. The control means 54 may perform temperature control by controlling the flow rate of the pump. In this case, the control means 54 may not include the temperature control means.

  Further, as shown in FIG. 2B, a side cut 10 is formed in the vicinity of the cylinder bore 2 on the screw rotation side wall surface of the raw material supply unit 4.

  Next, the melt-kneading of the pulverized film product in the twin-screw extruder of this embodiment will be described.

  First, the pulverized film as a raw material supplied from the hopper 51 to the chute 53 is supplied from the chute 53 to the raw material supply port 9. Next, the crushed film product supplied to the raw material supply port 9 is supplied to the rotating screw 1 while being guided by the undercut 7 and the side cut 10 below the downstream side stepped portion 20b.

For this embodiment, made to match the lower end 4c ₁ of the downstream wall 4c of the raw material supply section 4 against the top 20b ₁ of the downstream step portion 20b. By adopting such a configuration, the void (see FIG. 4B) seen in Patent Document 1 is eliminated, and the opening size ratio of the raw material supply port 9 is 1 / D = 4.0 to 9.5. Further, the angle β between the screw 1 and the undercut surface 7a is set in a range larger than 15 ° and not larger than 50 °.

  When the transport amount of the raw material in the upper gap 1a and the lower gap 1b, which are the gaps between the upper and lower sides of the screw 1 and the cylinder bore 2, is such that the upper gap 1a ≧ the lower gap 1b is full, the bite into the screw 1 In the case of the present embodiment, the upper gap 1a <the lower gap 1b is always satisfied by eliminating the void and expanding the opening area and setting the undercut angle within a suitable range. It is possible to achieve a relationship of starvation, and thus good biting can be realized.

  The film pulverized product supplied into the cylinder 52 as described above is transported in the downstream direction while being melt-kneaded by the two rotating screws 1.

  As described above, since the cylinder hopper 20 of the present embodiment provided with the raw material supply unit 4 can bite the raw material satisfactorily, the processing capacity of the raw material can be improved without increasing the rotational speed of the screw 1. it can. Since the raw material is melted and kneaded by the low rotation screw 1, yellowing of the resin due to an increase in the resin temperature can be prevented. Furthermore, since the cylinder hopper 20 of the present embodiment including the raw material supply unit 4 can realize good biting, even if the screw 1 is operated at a low rotation, it is difficult to generate a feed neck.

  Moreover, since the raw material supply unit 4 is controlled to an appropriate temperature by the cooling water, the pulverized film in contact with the wall surface of the raw material supply unit 4 is not softened. Thereby, the reduction | decrease of the substantial opening area by the adhesion to the raw material supply port 9 of the softened film ground product which has conventionally interfered with the raw material supply from a chute | shoot can also be suppressed.

Furthermore, since the cylinder hopper 20 of the present embodiment can cope with a pulverized film having a small bulk specific gravity, it can also cope with pellets having a larger bulk specific gravity than the pulverized film. For this reason, it is not necessary to prepare multiple cylinder hoppers according to the kind of raw material by using the cylinder hopper 20 of this embodiment.
(Example)
A comparative test of the ability to produce molten resin using a twin screw extruder using a pulverized film as a raw material was performed when the cylinder hopper of the present invention was used and when a conventional cylinder hopper was used. That is, the number of screw rotations required to discharge the same amount of molten resin and the resin temperature at that time were measured.

  The comparison results are shown in Table 1.

  The conventional cylinder hopper 1 shown in Table 1 is the type of cylinder hopper shown in FIG. 3 that does not have a raw material supply unit, and the conventional cylinder hopper 2 is a raw material in which a void is formed as shown in FIG. A cylinder hopper of the type provided with a supply unit.

  The opening size of the raw material supply port of the present invention is 1 / D = 5.0, where l is the size in the transport direction of the raw material and D is the outer diameter size of the screw 1, and 1 / D of the conventional cylinder hopper 1. = 2.0, l / D of the conventional cylinder hopper 2 is larger than 3.0.

  The opening size of the opening of the present invention is L / D = 7.0, which is larger than L / D = 2.5 of the conventional cylinder hopper 1 and L / D = 4.7 of the conventional cylinder hopper 2. is doing.

  Note that the angle between the undercut surface of each cylinder hopper and the screw is 30 °.

  A comparative test of the ability to produce a molten resin using a pulverized film having a bulk density of 0.02 g / cc to 0.05 g / cc as a raw material for a twin screw type extruder using the above cylinder hoppers was performed.

  As a result, the cylinder hopper of the present invention can produce a molten resin with a discharge rate of 200 kg / h even if the rotational speed of the screw is reduced to 90 rpm, and has to be operated at 290 rpm in order to achieve the same discharge rate. Compared with the rotational speed of the cylinder hopper 1, the rotational speed could be 1/3 or less. In addition, when the conventional cylinder hopper 1 is set to 290 rpm or less, it becomes impossible to stably supply raw materials due to the feed neck. Further, when the conventional cylinder hopper 2 was tested at a rotational speed down to 125 rpm, the raw material could not be stably supplied due to the feed neck at this rotational speed.

  When the discharge rate was 200 kg / h, the resin temperature rose to 285 ° C. for the conventional cylinder hopper 1 and to 255 ° C. for the conventional cylinder hopper 2. On the other hand, since the cylinder hopper of the present invention has a cooling mechanism, it rose only to 245 to 250 ° C. In addition, when the cylinder hopper of the present invention is used, even if the screw rotation speed is increased to 185 rpm in order to obtain a discharge rate of 300 kg / h, the resin temperature only rises to 265 ° C., and the raw material is stabilized without causing a feed neck. Could be supplied.

It is a block diagram of an example of the twin-screw type extruder of this invention. It is sectional drawing of an example of the cylinder hopper of this invention. It is the block diagram of an example of the block diagram of an example of the conventional twin-screw type extruder, and a cylinder hopper. It is the block diagram of the other example of the conventional biaxial screw type extruder, and the other example of a cylinder hopper.

Explanation of symbols

DESCRIPTION OF SYMBOLS 1 Screw 1a Upper side gap 1b Lower side gap 2 Cylinder inner hole 3 Opening part 4 Raw material supply part 4a Transport direction side surface 4b Upstream side wall 4c Downstream side wall 4c ₁ Lower end part 4c ₂ Inner surface 7 Undercut 7a Undercut surface 9 Raw material supply port 10 Side Cut 14 Jacket inlet 15 Jacket outlet 16 Flow path 20 Cylinder hopper 20a Upstream side step portion 20b Downstream side step portion 20b ₁ Top portion 20c Mounting portion 34 Raw material supply portion 50 Twin screw extruder 51 Hopper 52 Cylinder 53 Chute 54 Control means 55 Screw drive device

Claims (4)

Film crushing formed by crushing a resin film in the cylinder bore of a twin-screw type kneading and extruding machine having a cylinder in which a cylinder bore that accommodates two screws in parallel and rotatably is formed In a cylinder hopper that supplies a product as a raw material through a communication port and an opening communicating with the cylinder bore,
A downstream step (20b) having an undercut (7) formed in the lower portion is formed so as to protrude into the communication port (20D), and a raw material supply unit (4) having a raw material supply port (9) is formed. The communication port (20D) is formed so that the lower end (4c ₁ ) of the downstream side wall (4c) of the raw material supply unit (4) and the top (20b ₁ ) of the downstream side step (20b) match. Cylinder hopper characterized by being mounted inside.   When the dimension in the transport direction of the raw material is l and the outer diameter dimension of the screw (1) is D, the opening dimension ratio of the raw material supply port (9) is in the range of 1 / D = 4.0 to 9.5. The cylinder hopper according to claim 1, wherein the cylinder hopper is inside.   The cylinder hopper according to claim 1 or 2, wherein a flow path (16) for flowing a refrigerant is formed in a wall forming an outer periphery of the raw material supply port (9) of the raw material supply section (4). . The angle (β) between the undercut surface (7a) facing the cylinder inner hole (2) of the downstream side step (20b) and the rotational axis of the screw (1) is greater than 15 °, and The cylinder hopper according to any one of claims 1 to 3, which is within a range of 50 ° or less.

Images