Patent Application
20090110761
The present invention relates to an extrusion molding apparatus for a resin tube, designed to mold a tube used as a material for catheters or the like, by causing thermally melted resin being extruded from an extruder to pass through a die.
As for said extrusion molding apparatus for a resin tube, there have heretofore been ones shown in the following Patent Documents 1 and 2. According to these gazettes, said extrusion molding apparatus comprises extruders for thermally melting resins to enable the extrusion of the resins, and a die having tube molding passages causing the resins extruded from said extruders to forwardly pass therethrough to enable the molding of a tube.
And, during the operation of said extrusion molding apparatus, said extruders are driven so that thermally melted resins are extruded from the extruders. Thereupon, the resins pass through said tube molding passages, whereby a tube is molded.
Further, said extrusion molding apparatus enables automatic operation, wherein in order that the flow per unit time of the resin passing from the extruder to the tube molding passage may be incessantly changed, said flow is made adjustable. During this automatic operation, the flow of the resin being extruded from said extruder is changed. Thereupon, following this change, the flow of the resin passing through said tube molding passage is changed so as to enable the molding of a tube to desired dimensions, concerning wall thickness and diameter.
More specifically, for example, if the flow of the resin being extruded from said extruder is increased, the wall thickness of the tube molded at this time increases or the diameter increases. On the other hand, if the flow from said extruder is reduced, the wall thickness of the tube molded at this time becomes thinner or the diameter is reduced. And, in this manner, the molding of a tube is enabled such that any cross-section along the longitudinal direction has a desired dimension.
In this connection, the passage for resin flow from said extruder to the tube molding passage in the die has a large volume to a certain extent as a whole. And, during the operation of said extrusion molding apparatus, resin is filled in said passage.
During the automatic operation of said extrusion molding apparatus, if the flow of the resin being extruded from the extruder is increased, the resin in said passage is pressurized on the basis thereof, this pressure being transmitted as far as to the resin in said tube molding passage. Thereby, the flow of the resin going to pass through this tube molding passage tends to be increased.
Here, as described above, the passage has a large volume and is filled with resin, and the volume of the resin also increases. For this reason, this resin tends to be subjected to volumetric variation to greatly contract by the pressure from said extruder. Consequently, there is a possibility that the transmission of said pressure from said extruder to the tube molding passage may delay by an amount corresponding thereto. Particularly, when said resin is soft, said volumetric variation due to said pressure increases, leading to a possibility that the transmission of this pressure may further delay.
Further, as described above, the volume of the resin filled in the passage is large. For this reason, when the flow is changed in such a manner as to reduce the flow of the resin being extruded from the extruder, the resin in said passage tends to be subjected to volumetric variation such that it is expanded by the residual pressure. Consequently, even if the flow of the resin being extruded from the extruder is reduced, the flow of the resin passing through said tube molding passage does not become instantly reduced, that is, there is a possibility that problems may develop concerning responsiveness. Particularly, when said resin is soft, the volumetric variation further increases, making said problems concerning responsiveness more remarkable.
As a result, with the conventional extrusion molding apparatus, it is difficult to cause the change of the flow of the resin passing through said tube molding passage to follow with satisfactory responsiveness the change of the flow of the resin being extruded from the extruder. Thus, it is not easy to make more accurate the dimensional accuracy of the tube being molded.
With the above in mind, an object of the invention is to make more accurate the dimensions of a tube being molded by an extrusion molding apparatus.
Further, another object of the invention is to simplify the arrangement of the extrusion molding apparatus enabling the molding of the accurate tube described above.
Further, it is also an object to ensure that the molding of the accurate tube described above is easily performed.
The invention provides an extrusion molding apparatus for a resin tube, comprising an extruder for thermally melting the resin to enable the extrusion of the resin, and a die having a tube molding passage causing the resin extruded from said extruder to forwardly pass therethrough to enable the molding of a tube,
wherein there is provided a flow adjusting valve enabling the adjustment of the flow per unit time of the resin passing from the extruder to the tube molding passage.
In addition, added to the above invention, there is provided an extrusion molding apparatus for a resin tube with said die formed with an inflow passage enabling the resin being extruded from said extruder to flow into the rear of said tube molding passage, wherein
the degree of opening of said inflow passage may be made adjustable by said flow adjusting valve.
Further, in said invention, a communication passage for communicating the intermediate portion of said inflow passage to outside said die may be made openable/closable by said flow adjusting valve.
Further, in said invention, there may be provided an opening-degree adjusting valve enabling the adjustment of the opening degree of said communication passage.
Further, another invention provides an extrusion molding apparatus for a resin tube comprising a plurality of extruders for thermally melting and respectively extruding resins of different kinds, and a die provided with an inner layer tube molding passage for forwardly passing therethrough the resin extruded from one of these extruders to enable the molding of an inner layer tube, and an outer layer tube molding passage for forwardly passing therethrough the resin extruded from the other extruder to enable the molding of an outer layer tube which is to be externally fitted integrally on said inner layer tube, said die enabling the molding of a multi-layer tube by these inner and outer layer tubes,
wherein there are installed flow adjusting valves enabling the adjustment of each flow per unit time of each resin extruded from each extruder and passing to one of the inner and outer layer tube molding passages.
Further, in said another invention, inner and outer extrusion ports constituting the respective front ends of said inner and outer layer tube molding passages may be disposed radially close to each other and be opened forwardly from the front end of the die separately from each other.
Further, added to said another invention, there is provided an extrusion molding apparatus for a resin tube, with said die formed with a through-hole longitudinally extending through said die and passing inwardly of said inner layer tube molding passage, said tube being externally fitted on a core material forwardly passing through said through-hole, wherein
said inner extrusion port of said inner layer tube molding passage may be disposed close to the front end opening radially constituting the front end of said through-hole.
The effects by the invention are as follows.
In the invention, in an extrusion molding apparatus for a resin tube, comprising an extruder for thermally melting the resin to enable the extrusion of the resin, and a die having a tube molding passage causing the resin extruded from said extruder to forwardly pass therethrough to enable the molding of a tube,
there is provided a flow adjusting valve enabling the adjustment of the flow per unit time of the resin passing from said extruder to the tube molding passage.
For this reason, in the case of molding a tube by driving said extruder to cause the resin being extruded from this extruder to pass through said tube molding passage, the operation of said flow adjusting valve adjusts the flow of said resin. Thereupon, the wall thickness and diameter of said tube can be adjusted to desired values, providing a desired tube.
Here, the volume of the space in “passage” for resin flow extending from said flow adjusting valve to the tube molding passage is smaller than that of such passage extending from the extruder to the tube molding passage. For this reason, the volume of the resin filled in said “passage” becomes also small. Consequently, by the amount corresponding thereto the volumetric variation of said resin due to external force is suppressed such that it is small.
And, suppose that said flow adjusting valve is actuated so as to change the flow of the resin passing from said flow adjusting valve to said tube molding passage. In this case, as described above, the volume of the resin in the “passage” is small and volumetric variations due to external force are suppressed such that they are small. For this reason, the change of the flow of the resin passing through said tube molding passage follows the actuation of said flow adjusting valve with satisfactory responsiveness. Consequently, the dimensional accuracy of the tube being molded by the extrusion molding apparatus can be made more accurate.
In addition, added to said invention, there is provided an extrusion molding apparatus for a resin tube with said die formed with an inflow passage enabling the resin being extruded from said extruder to flow into the rear of said tube molding passage, wherein
the degree of opening of said inflow passage may be made adjustable by said flow adjusting valve.
Here, as described above, the die is formed with the tube molding passage, and the degree of opening of the inflow passage formed in said die is made adjustable by said flow adjusting valve. For this reason, this flow adjusting valve tends to pass close to said tube molding passage. Consequently, by an amount corresponding thereto the volume of said “passage” becomes further small, and so does the volume of the resin filled in this “passage.”
As a result, the change of the flow of the resin passing through said tube molding passage follows the actuation of said flow adjusting valve with satisfactory responsiveness. Consequently, the dimensional accuracy of the tube being molded by the extrusion molding apparatus can be made further accurate.
Further, said flow adjusting valve is used for adjusting the degree of opening of said inflow passage. Further, this inflow passage is formed in the die. For this reason, said flow adjusting valve can be simplified in arrangement by utilizing part of said die. In other words, said extrusion molding apparatus, though capable of accurately molding tubes, can be simplified in arrangement.
Further, in said invention, a communication passage for communicating the intermediate portion of said inflow passage to outside said die may be made openable/closable by said flow adjusting valve.
With the arrangement thus made, when said resin is passed from said extruder to said tube molding passage through the flow adjusting valve and said inflow passage, said flow adjusting valve causes part of the full flow extruded from said extruder to be discharged in a predetermined amount to outside the die through said communication passage. Thereupon, this enables the adjustment of the flow of the resin passed to said tube molding passage.
That is, even in the case of enabling the adjustment of the flow of the resin passed to said tube molding passage, the full flow extruded from the extruder can be made approximately constant. For this reason, whereas in the case of molding said tube to desired dimensions, trying to change the extrusion flow from the extruder would tend to make control troublesome, such control is unnecessary. Consequently, the molding of said accurate tube described above is facilitated.
Further, in said invention, there may be provided an opening degree adjusting valve which enables the adjustment of the degree of opening of said communication passage.
With the arrangement thus made, part of the flow of the resin discharged to outside the die through said communication passage can be adjusted to a desired value by the adjustment of the degree of opening of the communication passage by said opening degree adjusting valve. And, since such adjusting operation can be easily effected, the molding of the tube to desired dimensions can be effected further easily.
Further, another invention provides an extrusion molding apparatus for a resin tube comprising a plurality of extruders for thermally melting and respectively extruding resins of different kinds, and a die provided with an inner layer tube molding passage for forwardly passing therethrough the resin extruded from one of these extruders to enable the molding of an inner layer tube, and an outer layer tube molding passage for forwardly passing therethrough the resin extruded from the other extruder to enable the molding of an outer layer tube which is to be externally fitted integrally on said inner layer tube, said die enabling the molding of a multi-layer tube by these inner and outer layer tubes,
wherein there are installed flow adjusting valves respectively enabling the adjustment of each flow per unit time of each resin extruded from each said extruder and passed to one of said inner and outer layer tube molding passages.
With the arrangement thus made, in the case of molding a multi-layer tube by the driving of each said extruder to cause each resin extruded from each extruder to pass through each said tube molding passage, the flow of said resin can be adjusted by the actuation of each said flow adjusting valve. Consequently, the wall thickness and diameter of said inner and outer layer tubes can be adjusted to respective desired values, providing a desired multi-layer tube.
Here, the volume of the space in each “passage” for resin flow extending from each said flow adjusting valve to each tube molding passage is smaller than that of such “passage” extending from each extruder to each tube molding passage. For this reason, the volume of the resin filled in each said “passage” becomes also small. Consequently, by the amount corresponding thereto the volumetric variation of said resin due to external force is suppressed such that it is small.
And, suppose that each said flow adjusting valve is actuated so as to change the flow of the resin passing from each said flow adjusting valve to each said tube molding passage. In this case, as described above, the volume of the resin in each “passage” is small and volumetric variations due to external force are suppressed such that it is small. For this reason, the change of the flow of the resin passing through each said tube molding passage follows the actuation of each said flow adjusting valve with satisfactory responsiveness. Consequently, the dimensional accuracies of the inner and outer layer tubes of the multi-layer tube being molded by the extrusion molding apparatus can be respectively made further high.
Further, in said another invention, inner and outer extrusion ports constituting the respective front ends of said inner and outer layer tube molding passages may be disposed radially close to each other and be opened forwardly from the front end surface of the die separately from each other.
With the arrangement thus made, each resin being extruded from each said extruder by the driving of each said extruder is passed through each tube molding passage in said die, thereby molding inner and outer layer tubes. Further, when the inner and outer layer tubes are extruded forwardly of the die through said inner and outer extrusion ports, the outer layer tube is externally fitted on the inner layer tube, thereby molding an integral multi-layer tube.
In the above case, the inner and outer extrusion ports are disposed radially close to each other. For this reason, when said individual resins pass through the tube molding passages in said die and are forwardly extruded from said inner and outer extrusion ports, said inner and outer layer tubes immediately after being forwardly extruded from said inner and outer extrusion ports fit together and are smoothly integrated without requiring relatively large radial deformation.
Furthermore, as described above, the inner and outer extrusion ports are partly or wholly opened forwardly from the front end surface of said die separately from each other. For this reason, when said inner and outer layer tubes fit together, said inner and outer layer tubes are suppressed from pressing each other.
Consequently, said inner and outer layer tubes are prevented from being unintentionally deformed by mutual pressing. For this reason, the respective wall thicknesses of the inner and outer layers of the multi-layer tube molded by said extrusion molding apparatus can be respectively made more accurate.
Further, added to said another invention, there is provided an extrusion molding apparatus for a resin tube with said die formed with a through-hole longitudinally extending through said die and passing inwardly of said inner layer tube molding passage, said tube being externally fitted on a core material forwardly passing through said through-hole, wherein
said inner extrusion port of said inner layer tube molding passage may be disposed close to the front end opening radially constituting the front end of said through-hole.
With the arrangement thus made, by the driving of each said extruder, a multi-layer tube is molded as it is extruded from said die, and this tube is externally fitted on said core material, so that an intermediate product is molded using these tubes and the core material.
Here, as described above, the inner extrusion port is disposed radially close to said front end opening. Furthermore, as described above, the inner and outer extrusion ports are disposed radially close to each other. For this reason, when said tube is extruded from said inner extrusion port forwardly of said die, said inner and outer layer tubes immediately after they are extruded from said inner extrusion port are, without requiring large radial deformation, externally fitted on the core material immediately after slipping out of the front end opening in said through-hole.
Consequently, the multi-layer tube in said intermediate product molded by said extrusion molding apparatus can have the wall thicknesses of its inner and outer layer tubes respectively made accurate.
A best mode for carrying out the invention to realize an object which, relating to an extrusion molding apparatus for a resin tube according to the invention, is to make more accurate the dimensions of a tube molded by the extrusion molding apparatus, is as follows.
That is, the extrusion molding apparatus comprises an extruder for thermally melting resin to enable the extrusion of the resin, and a die having a tube molding passage for forwardly passing therethrough the resin extruded from said extruder to enable the molding of a tube. A flow adjusting valve is provided which enables the adjustment of flow per unit time of the resin passing from said extruder to the tube molding passage, and molding is performed such that the adjustment of the flow by the actuation of the flow adjusting valve enables the dimensions of various parts of said tube to be of desirable values.
To describe the invention in more detail, embodiments thereof will be described with reference to the accompanying drawings.
In
The extrusion molding apparatus 1 comprises a plurality (two) of first and second extruders 6 and 7 for thermally melting thermoplastic first and second resins 3 and 4 to enable their extrusion, a die 11 having inner and outer layer tube molding passages 9 and 10 through which the first and second resins 3 and 4 extruded from these first and second extruders 6 and 7 are separately forwardly passed to enable the molding of the inner and outer layer tubes 2a and 2b of said tube 2, a cold-curing device 13 for cold-curing by water said tube 2 molded by being passed through said inner and outer layer tube molding passages 9 and 10, and an electrically driven take-up device 14 for taking up said tube 2 cured by this cold-curing device 13, at a predetermined speed (for example, 2.5-10 m/min).
Said first and second resins 3 and 4 differ from each other in hardness at ordinary temperature. Further, the thermally melting of said first and second resins 3 and 4 is achieved by heating using a heater. Further, said first and second extruders 6 and 7 rotationally drive screws by an electric motor.
Said die will now be described in more detail. Said inner and outer tube molding passages 9 and 10 are each in the form of a forwardly tapering frustum and are disposed on the same axis 16. Further, in the radial direction (orthogonal direction, hereinafter the same) of this axis 16, the inner layer tube molding passage 9 is disposed inwardly of the outer layer tube molding passage 10. The respective front ends of said inner and outer layer tube molding passages 9 and 10 are constituted by inner and outer extrusion ports 17 and 18, these extrusion ports 17 and 18 extending substantially in parallel with axis 16. These inner and outer extrusion ports 17 and 18 enable said first and second resins 3 and 4 to be extruded forwardly which is outside said die 11. Said inner and outer extrusion ports 17 and 18 are disposed radially close to each other so as to be close to each other. Further, said inner and outer extrusion ports 17 and 18 are partly or wholly opened forwardly from the front end surface 19 of said die 11 and separately from each other.
Said die 11 is formed with first and second inflow passages 21 and 22. These inflow passages 21 and 22 enables the first and second resins 3 and 4 extruded from said first and second extruders 6 and 7 to flow into the respective rears of said inner and outer layer tube molding passages 9 and 10 separately from each other. In this case, the cross-sectional areas of the two inflow passages 21 and 22 are substantially the same. In addition, the cross-sectional area of the first inflow passage 21 may be made larger than that of the second inflow passage, and vise versa.
The first resin 3 extruded from the first extruder 6, which is one extruder 6 of said first and second extruders 6 and 7, is caused to flow into the rear of said inner layer tube molding passage 9 via said first inflow passage 21. And, thereafter, said resin 3 is passed through said inner layer tube molding passage 9 and extruded forwardly of said die 11, whereby said inner layer tube 2a is molded. Further, the second resin 4 extruded from the second extruder 7 which is the other extruder 7 is caused to flow into the rear of said outer layer tube molding passage 10 via said second inflow passage 22. And, thereafter, said resin 4 is passed through said outer layer tube molding passage 10 and extruded forwardly of said die 11, whereby said outer layer tube 2b is molded. In this case, this outer layer tube 2b is externally fitted integrally on said inner layer tube 2a. In other words, said first and second resins 3 and 4 are passed through the inner and outer layer tube molding passages 9 and 10 via said first and second inflow passages 21 and 22, whereby said tube 2 is molded.
A through-hole 24 of circular cross-section extending on said axis 16 is formed in said die 11. Said through-hole 24 longitudinally extends through said die 11 and is formed inwardly of said inner layer tube molding passage 9. A core material 25 of circular cross-section made of copper metal is allowed to forwardly pass through said through-hole 24. The inner diameter of said through-hole 24 is substantially equal to the outer diameter of said core material 25. And, the inner layer tube 2a of said tube 2 is externally fitted on the core material 25 passing forwardly in said through-hole 24, and said inner layer tube 2a can closely adhere to said core material 25. Disposed radially of said axis 16 and in the vicinity of the front end opening 26 constituting the front end of said through-hole 24 is the inner extrusion port 17 of said inner layer tube molding passage 9.
Installed on said axis 16 is another die 30 having a die hole 29 communicating with the extrusion ports 17 and 18 of said tube molding passages 9 and 10. This another die 30 is removably fixed to the front end surface 19 of said die 11 by a fastener 31.
First and second flow adjusting valves 34 and 35 are installed. These first and second flow adjusting valves 34 and 35 make it possible to separately adjust the respective flows per unit time (m3/min: hereinafter referred to simply as flows) of the first and second resins 3 and 4 extruded from said first and second extruders 6 and 7 and passed to said inner and outer layer tube molding passages 9 and 10.
Further, said flow adjusting valves 34 and 35 adjust the degrees of opening of said inflow passages 21 and 22 to make it possible to adjust the flows of the resins 3 and 4. Concretely, said flow adjusting valves 34 and 35 each comprise a valve main body 36 constituted by part of said die 11, a columnar valve body 39 fitted in a circular valve body fit hole 37 to divide the longitudinal intermediate portion of each of the inflow passages 21 and 22, in such a manner as to allow its turn R around the axis 38, and an actuator 40, such as an air cylinder, which enables this valve body 39 to make turn R to a predetermined turn position. The valve bodies 39 are formed with first and second valve holes 41 and 42 radially extending therethrough and independent of each other. Formed in each valve body 39 is a communication passage 43 communicating the intermediate portion of said second valve hole 42 to outside the die 11. Further, there is installed a needle valve type opening degree adjusting valve 44 which makes it possible to manually adjust the degree of opening of said communication passage 43.
The electric motors for said extruders 6 and 7 and take-up device 14, and actuators 40 are connected to an electronic controller and automatically controlled according to a predetermined program. Here, said extruders 6 and 7 are driven such that when the pressures of the resins 3 and 4 immediately after their extrusion have predetermined values, the flows of the resins 3 and 4 extruded from the extruders 6 and 7 are substantially constant.
When the flow adjusting valves 34 and 35 are actuated by the driving of said actuators 40, said valve body 39 is turned as at R. And, when this valve body 39 is positioned at “full open position” (in
On the other hand, when the driving of said actuator 40 positions said valve body 39 at “half-open position” (in
Further, though not illustrated, when said valve bodies 39 are positioned at “full close position” by the driving of said actuators 40, the first and second valve holes 41 and 42 are closed by the inner peripheral surfaces of the valve body fit holes 37. In other words, said inflow passages 21 and 22 are fully closed. Thereupon, the flows of the resins 3 and 4 extruded from the extruders 6 and 7 and passed to the tube molding passages 9 and 10 are reduced to zero. In other words, in this manner, the degrees of opening of the inflow passages 21 and 22 are made adjustable.
Further, as described above, when the valve bodies 39 are positioned at said “half open position” by the driving of the actuators 40, the communication passages 43 which communicate the intermediate portions of the inflow passages 21 and 22 to outside the die 11 are opened.
When the valve bodies 39 are shifted from this state to said “full open position” or “full close position,” the communication passages 43 are closed.
In the case of molding the tube 2 by operating the extrusion molding apparatus 1, first, the extruders 6 and 7 and the take-up device 14 are driven. Further, in this case, the actuators 40 for the flow adjusting valves 34 and 35 are made able to be driven. The resins 3 and 4 extruded from the extruders 6 and 7 attending said driving pass through the inflow passages 21 and 22 and flow adjusting valves 34 and 35 to the inner and outer layer tube molding passages 9 and 10. And, the resins 3 and 4 are passed through the inner and outer layer tube molding passages 9 and 10 and extruded forwardly of the die 11, whereby the inner and outer layer tubes 2a and 2b are molded. Further, when these inner and outer layer tubes 2a and 2b are extruded from the extrusion ports 17 and 18, the outer layer tube 2b is externally fitted on the inner layer tube 2a and they are integrally fixed to each other, so that the multi-layer tube 2 is molded.
Further, simultaneously with the molding of the tube 2, the core material 25 is forwardly passed through the through-hole 24. In the front vicinity of the extrusion ports 17 and 18 and front end opening 26, the core material 25 has externally fitted thereon the inner layer tube 2a of the tube 2, with the inner peripheral surface of the inner layer tube 2a being closely adhered thereto. Thereby, an intermediate product 47, which is a combination of the tube 2 and the core material 25, is molded. This intermediate product 47 is passed through another die 30, whereby molding is effected such that any cross-section of the tube 2 is perfectly circular and the outer diameter is constant. Further, thereafter, the intermediate product 47 is cold-cured by the cold curing device 13.
In
Reversely to the above, the valve body 39 of said first flow adjusting valve 34 is put in “half open position.” Further, the valve body 39 of said second flow adjusting valve 35 is put in “full open position.” Thereupon, by the action reverse to the above, the tube 2, as shown by C in
As described above, in the case of putting the valve body 39 in “half open position,” each of the flows of the resins 3 and 4 passed from the extruders 6 and 7 to the tube molding passages 9 and 10, is the reminder flow (Q2=QT−Q1). However, since the partial flow (Q1) is discharged through said communication passage 43, the variation of the full flow (QT) of each of the resins 3 and 4 extruded from the extruders 6 and 7 is suppressed, and it is substantially constant. Here, when said valve body 39 is to be switched to either “full open position” or “half open position,” more or less time is required for the turn R of the valve body 39. For this reason, as shown by B and D in
Referring to
In the above case, another die 30 does not exist. For this reason, the front vicinity of the extrusion port 18 constituting the front end of said outer layer tube molding passage 10 is opened radially outward of said axis 16. Consequently, the outer diameter of the outer layer tube 2b can be made greater than that of the inner layer tube 2a. In other words, the outer diameter of the tube 2 can be adjusted to desired dimension at any longitudinal section. Further, the portions B and D in
Said intermediate product 47 is used as a material, for example, of catheters. That is, said intermediate product 47 is cut at predetermined longitudinal positions and into predetermined lengths by an unillustrated cutter. Thereafter, said core material 25 is longitudinally stretched by a stretching means, thereby being reduced in radial dimension. Then, this core material 25 is extracted from said tube 2 so as to separate said core material 25 from the inner peripheral surface of the inner layer tube 2a of said tube 2, whereupon said catheter is molded.
Here, the first resin 3 of which the inner layer tube 2a of said tube 2 is molded differ in hardness from the second resin 4 of which the outer layer tube 2b is molded. For this reason, as shown in
According to the above arrangement, the extrusion molding apparatus 1 comprises extruders 6 and 7 for thermally melting resins 3 and 4 to enable extrusion thereof, and a die 11 having tube molding passages 9 and 10 for forwardly passing therethrough the resins 3 and 4 extruded from the extruders 6 and 7 to make it possible to mold a tube 2, wherein flow adjusting valves 34 and 35 are installed which make it possible to adjust the flow per unit time of each of the resins 3 and 4 passing from said extruders 6 and 7 to the tube molding passages 9 and 10.
For this reason, in the case of molding the tube 2 by passing the resins 3 and 4, which are extruded from the extruders 6 and 7 by the driving of the extruders 6 and 7, through said tube molding passages 9 and 10, the flows of said resins 3 and 4 are adjusted by the actions attending the operation of said flow adjusting valves 34 and 35. Thereupon, the wall thickness and radial dimension of said tube 2 can be adjusted to desired values, so that a desired tube 2 is obtained.
Here, the volumes of the spaces in the “passages” for the flowing of the resins 3 and 4 extending from said flow adjusting valves 34 and 35 to the tube molding passages 9 and 10 is smaller than those extending from the extruders 6 and 7 to the tube molding passages 9 and 10. For this reason, the volumes of the resins 3 and 4 filling said “passages” are also small. Consequently, by an amount corresponding thereto, the volumetric variations of said resins 3 and 4 due to external force are suppressed such that they are small.
And, suppose that said flow adjusting valves 34 and 35 are actuated so as to change the flows of the resins 3 and 4 passing from said flow adjusting valves 34 and 35 to said tube molding passages 9 and 10. In this case, as described above, the volumes of the resins 3 and 4 in the “passages” are small and volumetric variations due to external force are suppressed such that they are small. For this reason, the changes of the flows of the resins 3 and 4 passing through said tube molding passages 9 and 10 follow the actuation of said flow adjusting valves 34 and 35 with satisfactory responsiveness. Consequently, the dimensional accuracy of the tube 2 being molded by the extrusion molding apparatus 1 can be made more accurate.
Further, as described above, said die 11 is formed with inflow passages 21 and 22 enabling the resins 3 and 4 extruded from the extruders 6 and 7 to flow into the rears of said tube molding passages 9 and 10, and the degrees of opening of said inflow passages 21 and 22 are made adjustable by said flow adjusting valves 34 and 35.
Here, the die 11 is formed with the tube molding passages 9 and 10 as described above, and the degrees of opening of the inflow passages 21 and 22 formed in said die 11 are made adjustable by said flow adjusting valves 34 and 35. For this reason, the flow adjusting valves 34 and 35 tend to be close to said tube molding passages 9 and 10. Consequently, the volumes of said “passages” become further small, and so do the volumes of the resins 3 and 4 filled in the “passages.”
As a result, the changes of the flows of the resins 3 and 4 passing through said tube molding passages 9 and 10 follow the actuation of said flow adjusting valves 34 and 35 with satisfactory responsiveness. Consequently, the dimensional accuracy of the tube 2 being molded by the extrusion molding apparatus 1 can be made further accurate.
Further, said flow adjusting valve 34 and 35 are used for adjusting the degrees of opening of said inflow passages 21 and 22. Further, the inflow passages 21 and 22 are formed in the die 11. For this reason, said flow adjusting valves 34 and 35 can be simplified in arrangement by utilizing part of said die 11. In other words, said extrusion molding apparatus 1, though capable of accurately molding the tube 2, can be simplified in arrangement.
Further, as described above, the communication passage 43 for communicating the intermediate portions of said inflow passages 21 and 22 to outside said die 11 may be made openable/closable by said flow adjusting valves 34 and 35.
For this reason, when the resins 3 and 4 are passed from said extruders 6 and 7 through said flow adjusting valves 34 and 35 and said inflow passages 21 and 22 to said tube molding passages 9 and 10, the partial flows (Q1) of the full flows (QT) extruded from the extruders 6 and 7 are discharged in predetermined amounts to outside the die 11 through said communication passages 43 by said flow adjusting valves 34 and 35. Thereupon, this enables the adjustment of flows (remainder flows (Q2)) of the resins 3 and 4 passed to the tube molding passages 9 and 10.
That is, even in the case where the flows of the resins 3 and 4 passed to said tube molding passages 9 and 10 are made adjustable, the full flows (QT) extruded from the extruders 6 and 7 can be made substantially constant. Here, whereas in the case of molding said tube 2 to desired dimensions, trying to change the extrusion flows from the extruders 6 and 7 would tend to make control troublesome, such control is unnecessary. Consequently, the molding of said accurate tube 2 described above is facilitated.
Further, as described above, there are installed opening-degree adjusting valves 44 which enable the adjustment of the degree of opening of the communications passages 43.
For this reason, the partial flows (Q1) of the resins 3 and 4 discharged to outside the die 11 through said communication passages 43 can adjusted to desired values by the adjustment of the degree of opening of the communication passages 43 due to said opening-degree adjusting valves 44. And, since such adjusting operation can be easily performed, the molding of the tube 2 of desired dimensions can be further facilitated.
Further, as described above, there are installed flow adjusting valves 34 and 35 which enable the adjustment of the respective flows per unit time of the resins 3 and 4 extruded from the extruders 6 and 7 and passed to said inner and outer layer tube molding passages 9 and 10.
For this reason, in the case of molding a multi-layer tube 2 by the driving of said extruders 6 and 7 to cause resins 3 and 4 extruded from the extruders 6 and 7 to pass through said tube molding passages 9 and 10, the flows of said resins 3 and 4 can be adjusted by the actions attending the operation on said flow adjusting valves 34 and 35. Consequently, the wall thicknesses and radial dimensions of said inner and outer layer tubes 2a and 2b can be adjusted to respective desired values, providing a desired multi-layer tube 2.
Here, the volumes of the spaces in the “passages” for the flowing of the resins 3 and 4 extending from said flow adjusting valves 34 and 35 to the tube molding passages 9 and 10 are smaller than those extending from the extruders 6 and 7 to the tube molding passages 9 and 10. For this reason, the volumes of the resins 3 and 4 filled in said “passages” become also small. Consequently, by the amount corresponding thereto the volumetric variations of said resins 3 and 4 due to external force are suppressed such that they are small.
And, suppose that said flow adjusting valves 34 and 35 are actuated so as to change the flows of the resins 3 and 4 passing from said flow adjusting valves 34 and 35 to said tube molding passages 9 and 10. In this case, as described above, the volumes of the resins 3 and 4 in the “passages” are small and volumetric variations due to external force are suppressed such that they are small. For this reason, the changes of the flows of the resins 3 and 4 passing through said tube molding passages 9 and 10 follow the actuation of said flow adjusting valves 34 and 35 with satisfactory responsiveness. Consequently, the dimensional accuracies of the inner and outer layer tubes 2a and 2b of the multi-layer tube 2 being molded by the extrusion molding apparatus 1 can be respectively made further high.
Further, as described above, the inner and outer extrusion ports 17 and 18 constituting the respective front ends of the inner and outer layer tube molding passages 9 and 10 are disposed close to each other radially of said axis 16, and are opened forwardly from the front end surface 19 of the die 11 separately from each other.
For this reason, the resins 3 and 4 extruded from the extruders 6 and 7 by the driving of the extruders 6 and 7 are passed through the tube molding passages 9 and 10 of the die 11, thereby molding the inner and outer layer tubes 2a and 2b. Further, when the inner and outer layer tubes 2a and 2b, which are extruded from said inner and outer extrusion ports 17 and 18, forwardly of the die 11, the outer layer tube 2b is externally fitted integrally on the inner layer tube 2a, so that a multi-layer tube 2 is molded.
In the above case, the inner and outer extrusion ports 17 and 18 are disposed radially close to each other. For this reason, when said resins 3 and 4 are passed through the tube molding passages 9 and 10 of said die 11 and extruded forwardly from the inner and outer extrusion ports 17 and 18, said inner and outer layer tubes 2a and 2b, said inner and outer layer tubes 2a and 2b immediately after they are forwardly extruded from said inner and outer extrusion ports 17 and 18 fit together without requiring relatively large radial deformation, and smoothly integrated.
Furthermore, as described above, the inner and outer extrusion ports 17 and 18 are partly or wholly opened forwardly from the front end surface 19 of said die 11 separately from each other. For this reason, when said inner and outer layer tubes 2a and 2b fit together, these inner and outer layer tubes 2a and 2b are suppressed from pressing each other.
Consequently, said inner and outer layer tubes 2a and 2b are prevented from being unintentionally deformed by mutual pressing. For this reason, the respective wall thicknesses of the inner and outer layers of the multi-layer tube 2 molded by said extrusion molding apparatus 1 can be respectively made more accurate.
Further, said inner and outer extrusion ports 17 and 18 extend along said axis 16 and substantially in parallel with each other.
For this reason, when said inner and outer layer tubes 2a and 2b immediately after they are forwardly extruded from said inner and outer extrusion ports 17 and 18 fit together, these inner and outer layer tubes 2a and 2b are more reliably suppressed from pressing each other. Consequently, said inner and outer layer tubes are prevented from being unintentionally deformed by mutual pressing. As a result, the respective wall thicknesses of said inner and outer layer tubes 2a and 2b can be made further accurate.
Further, as described above, said die 11 is formed with a through-hole 24 longitudinally extending through said die 11 and passing inwardly of said inner layer tube molding passage 9, said tube 2 being externally fitted on a core material 25 forwardly passing through said through-hole 24, and said inner extrusion port 17 of said inner layer tube molding passage 9 is disposed close to the front end opening 26 constituting the front end of said through-hole 24 radially of said axis 16.
For this reason, extruded from said die 11 by the driving of said extruders 6 and 7, a multi-layer tube 2 is molded, this tube 2 being externally fitted on said core material 25, thus molding an intermediate product 47 using the tube 2 and the core material 25.
Here, as described above, the inner extrusion port 17 is disposed radially close to said front end opening 26. Furthermore, as described above, the inner and outer extrusion ports 17 and 18 are disposed radially close to each other. For this reason, when said tube 2 is extruded from said inner extrusion port 17 forwardly of the die 11, said inner and outer layer tubes 2a and 2b immediately after they are extruded from said inner extrusion port 17 are, without requiring large radial deformation, externally fitted on the core material 25 immediately after slipping out of the front end opening 26 in said through-hole 24.
Consequently, the multi-layer tube 2 in said intermediate product 47 molded by said extrusion molding apparatus 1 can have the respective wall thicknesses of its inner and outer layer tubes 2a and 2b made more accurate.
In addition, what has so far been described is by way of illustrated examples. Said tube 2 and tube molding passages 9 and 10 may be single-layered or three- or more-layered. Further, any one of the inner and outer layer tubes 2a and 2b of the tube 2 may have its hardness increased. Further, a gear pump may be interposed between said extruders 6 and 7 and die 11. Further, said flow adjusting valves 34 and 35 may be interposed between said extruders 6 and 7 and die 11.
Further, the invention may be achieved by suitably combining individual component members described above.
| Number | Date | Country | Kind |
|---|---|---|---|
| 2003-303095 | Aug 2003 | JP | national |
| Filing Document | Filing Date | Country | Kind | 371c Date |
|---|---|---|---|---|
| PCT/JP04/06655 | 5/18/2004 | WO | 00 | 2/27/2006 |
