CN100455427C - Multi-layer blown film molding machine and method of molding multi-layer blown film - Google Patents
Multi-layer blown film molding machine and method of molding multi-layer blown film Download PDFInfo
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- CN100455427C CN100455427C CNB2004800239572A CN200480023957A CN100455427C CN 100455427 C CN100455427 C CN 100455427C CN B2004800239572 A CNB2004800239572 A CN B2004800239572A CN 200480023957 A CN200480023957 A CN 200480023957A CN 100455427 C CN100455427 C CN 100455427C
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Abstract
A multi-layered blown film forming apparatus contains an adapter provided to supply a multiple types of resins, a forming die provided on a downstream side in an axial direction of the adapter, and a temperature controller mechanism. Molten resins of multiple types are individually fed to the forming die through the adapter. The forming die contains a main body, a multi-layer structure of a plurality of single-layer thin film dies disposed in an inner portion of the main body in an axial direction to produce a plurality of resin thin films corresponding to the molten resins of the multiple types, and a first annular path formed between main body and the multi-layer structure. A multi-layered thin film in which the plurality of resin thin films are overlaid is passed through the first annular path and is outputted as a multi-layered thin annular film. The temperature controller mechanism controls individual temperatures of the plurality of single-layer thin film forming dies independently.
Description
Technical field
The present invention relates to the film shaped method of multilayer blow moulding film shaping machine and multilayer blow moulding.
Background technology
Resin film is widely used, and in the technology that this resin film is produced in batches, seeks the high speed and the high-precision THICKNESS CONTROL of formation speed.As this techniques of mass production, known inflation film forming machine with ring-type extrusion finishing die, wherein, send into air to the cylinder resin molding inside that extrudes from finishing die, it is expanded, and the cylindric resin molding sealing of using niproll to expand, with the film bubble cooling that forms.Like this, make film article as inflation film.As the cooling technology of inflation film, the known forced cooling water that the nature cooling is arranged, utilize the pressure air that carries out from the air of gas nozzle injection to cool off, utilize cooling water to carry out cools off, utilizes air and water-cooled two-stage to force cooling.
At United States Patent (USP) 3,337, disclose the multilayer blow moulding film shaping machine that forms plural layers by multilayer ground extrusion film in No. 914 (first conventional example) and the United States Patent (USP) 4,798, No. 526 (second conventional examples).The multilayer blow moulding film shaping machine has the multistage model block (type Block ロ Star Network) that a plurality of resins are extruded annularly, has the advantage that can increase the number of plies by the exponent number that increases this model block.But, in the multilayer blow moulding film shaping machine of this multistage model structure, owing between multistage model block, have difference of height, therefore, for make being provided with highly to align the converter pipe arrangement is set on extruder corresponding to the extruder on each rank.Owing to need this converter pipe arrangement, so the structure complicated of the multilayer blow moulding film shaping machine of multistage model structure.
As other example,, disclose helically in No. 861 (the 3rd conventional example) and constitute the multilayer blow moulding film shaping machine that multistage resin is supplied with the multistage model structure on road at United States Patent (USP) 3,966.The forming machine of this conventional example is surpassing under the situation of five layers and multistageization, and the external diameter of mould has excessive tendency, sees in the miniaturization this point, lacks practicality, and is difficult to multistage ground and supplies with multiple molten resin respectively equably.
Drive the forming machine that discloses the order and the number of plies that can change layer structure simply in the flat 7-1579 communique (the 4th conventional example) the spy.As shown in Figure 1, mould 301 has the supply module 302-1 of a plurality of mortar shapes of same shape roughly, 2,3,4 multiple-rank arrangement.The a plurality of axial passageway 303 corresponding with each rank are configured in apart from axial line same position place, with the equal angles arranged spaced on a circumference.In such known technology, can change the number of plies more easily by changing the module number, and can change the order of layer structure by the relative angle that changes module, but towards discharge pressure gap 304, in fact become outward radially, supply with and can carry out with height general in the mold foundation 306 via supplying with road 305 by whole resins from axial line for resin flow.
In the disclosed technology of the 4th conventional example, be the cooling of the film that extrudes, need to be provided with the hole in a plurality of big footpaths of the module by each layer of mould, make the configuration complexity of supply passageway of molten resin.In addition, because the air by air flue is mold cools down, so have the reversal of effect that the resin with not at all easy heating and melting cools off again.In addition, flow through a large amount of air that is used to cool off, be difficult to be used to keep the fine setting of bubble diameter.Process towards floor supply port from the mold center owing to shift the supply road, so be difficult to supply with resin to each supply port equably centroclinally.
Open in 2002-79576 number technology in (the 5th conventional example) being disclosed in the spy, the hole in a plurality of big footpaths by the module shown in the 4th conventional example is replaced as the hole of the path that extends vertically.Thus, in the cooling that suppresses module, the adjusting of the relative bubble diameter of air pressure becomes easily, in addition, will supply with the road towards the transfer of the inclination at floor supply port center and process the supply road that changes to horizontal direction.
Using under the situation of flat model, is different owing to supply with the link position of extrusion mouth of the extruder of molten plastic on each of each layer of type tool, thus extruder highly difference is set.Be the highly alignment that is provided with, be provided with the converter pipe arrangement in the outlet of extruder with extruder.Supplying with under the situation of resin from the side, owing to supply with resin from the circumference side of mould, so be difficult to make resin to distribute equably.
Like this, the multilayer blow moulding film shaping machine of the prior art structures that heat from the outside of resin supply module that adopt more, model is in contact with one another.Under the situation of plural layers, concerning each film, its fusion point, softening point, optimum treatmenting temperature difference in this heating arrangement, are difficult to be adjusted to the temperature that is suitable for each thin-film material.
As shown in Figure 2, two-stage is forced cooling technology, on the multi-layer resinous cylindrical thin-film 202 that extrudes from plural layers forming model 201, carry out phase I cooling by the cooling air that blows out from ring-type gas nozzle 203 downwards, cool off the cooling water that air cooled multi-layer resinous cylindrical thin-film 202 flows down by the cooling water nozzle 204 from ring-type by this and carry out the second stage cooling.The cooling water that flows down from cooling water nozzle 204 is cooled to proper temperature by heat exchanger 205, and its flow is regulated by flow control valve 206.Like this, the detection and the FEEDBACK CONTROL of the overflow height of the water yield by carrying out cooling water, its temperature, downflow weir can be with cooling effectiveness and cooling performance optimizations.
In the inflation film manufacturing technology that is disclosed in special public clear 60-26010 number (the 6th conventional example), above water cooling plant that the bubble of the tubular film that will extrude from circular die cools off, be provided with gas blowing out device and gas suction device.Gas suction device sucks the warm braw that blows out from the gas blowing out device, makes this film bubble cooling.By forming gas flow, with the shape stability raising of film bubble from the slyness around the film bubble.
In being disclosed in the inflation film manufacturing technology that the spy opens flat 9-109274 number (the 7th conventional example), by air the tubular film that extrudes from mould is expanded, enclose air and also be configured as film blister formed products.Adopt drip washing as water-cooling pattern, after with this film foam forming product cooling, pressurize by warmed-up pinch roll.Like this, the mutual heat of film is fused, make a slice film.The warpage wide cut of annular membrane is directly as the width of film article, and the UTILIZATION OF VESIDUAL HEAT IN when film is extruded realizes high-speed production in heat of solution.
In such inflation film manufacturing technology, under the situation that this film is made with a kind of material, do not encounter problems, but the various kinds of resin material is layeredly being extruded and making under the situation of plural layers, kind corresponding to resin, their melting point, crystallized temperature difference, in being disclosed in the cooling technology of prior art, produce because the stress that the deformation of film resin storeroom causes produces on this resin film curling (deflection).If cooling velocity is inappropriate, then the crystallization of material resin is strengthened, and produces cloud and mist (smog), as commodity, and residue problem aspect its quality.
In the film bubble cooling technology of the 6th conventional example, around the film bubble, form gas flow sleekly, improve the shape stability of film bubble, but the film bubble after just being extruded by high temperature is soft, its hot strength is low.Therefore, when blowing out high-speed gas near the outlet of mould (mold), this film bubble shape easy deformation for keeping its stability, blows out speed and must reduce, and makes cooling effect reduce.
In being disclosed in the inflation film manufacturing technology of the 7th conventional example, the inner face of the air bubble-shaped film of ring-type is flatly pushed, and is undertaken bonding by heating.Under the low situation of the temperature of the la m resin of the film that various kinds of resin is formed stratiform, it is easy to manufacture.In addition, film article is because symmetry in the table, so inner deformation is cancelled out each other, has and deformational stress and curling few advantage can not occur.But owing to form multilayer, thereby in the characteristic of each layer resin material, promptly there is difficult point in the thermal bonding aspect of the intensity of Biao Mian smoothness, color, middle side, gas barrier and the inside.In this method for making technology, use the purpose of drip washing to be, be cooled to enough temperature for the hot strength that keeps the film bubble to a certain extent, but can not realize chilling or improve membrane quality.
It is important making the height alignment of extruder.In addition, it also is important setting up module easily.The special requirement temperature is fit in each layer unit.With single ground of multistage model structure rigid bodyization, and single this rigid body is carried out temperature control is important.Seek to produce the characteristic of multiple stratification resin, and minimizing is curling, does not have smog, the transparency is good.
Summary of the invention
The objective of the invention is to, height alignment that makes extruder and the multilayer blow moulding film shaping machine and the film shaped method of multilayer blow moulding of setting up module easily are provided.
Another object of the present invention is to, multilayer blow moulding film shaping machine and the film shaped method of multilayer blow moulding that can suitably control temperature in each layer unit are provided.
Another purpose of the present invention is, provides single ground of multistage model structure rigid bodyization is also carried out temperature controlled multilayer blow moulding film shaping machine and the film shaped method of multilayer blow moulding to this rigid body singlely.
Other purposes of the present invention are, the characteristic that generates the multiple stratification resin is provided, and curl less and do not have the transparent good multilayer blow moulding film shaping machine and the film shaped method of multilayer blow moulding of smog.
In the solution of the present invention, the multilayer blow moulding film shaping machine has: converter, and it supplies with various kinds of resin; Finishing die, it is located at the axial downstream of described converter; Temperature control device.Described multiple molten resin is individually supplied with to described finishing die via converter.Described finishing die has: main body; The laminate of a plurality of single thin film finishing dies, described a plurality of single thin film finishing dies in the inside of described main body, are created on the film of described resin corresponding in the described multiple molten resin along described axial arrangement; First annulus, it is formed between described main body and the described laminate.Lamination has the plural layers of a plurality of described films to export as the plural layers annular membrane by described first annulus, and described temperature control device is controlled each temperature of described a plurality of single thin film finishing dies independently.
At this, described temperature control device also can have: a plurality of cartridge heaters, and it connects described laminate and is provided with; At least one temperature sensor, it is located on each of described a plurality of single thin film finishing dies of described laminate; Control circuit, it is based on distinguish the described a plurality of cartridge heaters of drive to each temperature of setting of described a plurality of single thin film finishing dies with by the detected temperature of described temperature sensor, to heat single thin film finishing die corresponding in described a plurality of single thin film finishing die respectively by described a plurality of cartridge heaters.
Described temperature control device also has the cooling gas supply pipe, this gas supply pipe connects described laminate setting, discharge is used to cool off each cooling gas of described a plurality of single thin film finishing dies, and described control circuit also can be controlled described cooling from gas supply pipe to described cooling that supply with the amount with gas.
Each of described a plurality of single thin film finishing dies also can have upstream side individual layer finishing die and downstream individual layer finishing die.Between described upstream side individual layer finishing die and described downstream individual layer finishing die, form the ring-type path of cool air, flow through described ring-type path of cool air by making with gas from the described cooling of described tempering air supply pipe, thereby with described upstream side individual layer finishing die and the cooling of downstream individual layer finishing die.
The multilayer blow moulding film shaping machine also has rack body, and this rack body is located at the bottom of described finishing die and is had cradle portion, and this cradle portion has second annulus that is connected with described first annulus, to export described plural layers.Described temperature control device also has: airtrapping portion, and it is located between described rack body and the described laminate; Film bubble air supply pipe, it connects described laminate and arrives described airtrapping portion, is used for the delivery film bubble gas to described airtrapping portion; Gas nozzle, it connects described cradle portion and arrives described airtrapping portion, the described film bubble gas to discharge described airtrapping portion from the inside of the described plural layers of described second annulus output in.Described control circuit is controlled the amount of the described film bubble gas supplied with to described airtrapping portion via described film bubble air supply pipe.
The multilayer blow moulding film shaping machine can also have cooling body, and this cooling body is located at the downstream of described finishing die, is used to cool off described plural layers annular membrane.
Described cooling body has: first cooling body, and it is used to cool off described plural layers annular membrane; Second cooling body, it is located at the downstream of described first cooling body, cools off described plural layers annular membrane by the ring-type cooling water flow; The 3rd cooling body, it is located at the downstream of described second cooling body, by the spraying of cooling water described plural layers annular membrane is cooled off.
Described first cooling body has: air supply pipe, and it supplies with described cooling air stream to described ring-type air blow-off outlet, to be used to cooling air stream from ring-type air blow-off outlet with described plural layers annular membrane air cooling; Air regulator, it is located in the described air supply pipe, regulates the air mass flow of described cooling air; Heat exchanger is used in the air cooling, and it is located in the described air supply pipe, cools off described air.
Described second cooling body has: the first cooling water supply pipe, and it supplies with first cooling water; The first cooling water flow adjuster, it is located in the described first cooling water supply pipe, regulates the flow of described first cooling water; The first cooling water heat exchanger, it is located in the described first cooling water supply pipe, cools off described first cooling water; Reservoir, it stores described first cooling water.Described reservoir has the weir that can regulate from the water surface elevation of described first cooling water, and it is located at the inboard top of described reservoir, so that described first cooling water is as the overflow of described ring-type cooling water flow.
Described the 3rd cooling body also can have: a plurality of sprayers, its be located at described plural layers annular membrane around, second cooling water of spraying; The second cooling water supply pipe, it supplies with described second cooling water to described a plurality of sprayers; The second cooling water flow adjuster, it is located in the described second cooling water supply pipe, regulates second cooling water flow of described second cooling water; The second cooling water heat exchanger, it is located in the described second cooling water supply pipe, cools off described second cooling water.
Described a plurality of single thin film finishing die has same size, and each of described a plurality of single thin film shaping dies has the upstream side individual layer finishing die of truncated cone shape and engage the downstream individual layer finishing die of the truncated cone shape that also combines in the downstream with described upstream side individual layer finishing die.Described upstream side individual layer finishing die and described downstream individual layer finishing die have recess in the bottom, the described recess of described downstream individual layer finishing die and described upstream side individual layer finishing die is chimeric, described upstream side individual layer finishing die receives described resin corresponding in the described multiple molten resin, supply with to described downstream individual layer finishing die, described downstream individual layer finishing die has radial resin passage and the helical form resin passage that is formed at described frustum of a cone side and is connected with described radial resin passage, will output to described first annulus from the described resin of described upstream side individual layer finishing die via described radial resin passage and described helical form resin passage.
In other scheme of the present invention, the film shaped method of multilayer blow moulding realizes by following steps, that is: the temperature of each of a plurality of single thin film finishing dies of independent control; Finishing die has main body and at the laminate of described body interior along described a plurality of single thin film finishing dies of described axial arrangement, by converter multiple molten resin is supplied with to described a plurality of single thin film finishing dies respectively; Generate the film of described resin corresponding in the multiple molten resin by each of described a plurality of described single thin film finishing dies; Make lamination plural layers from the described film of described a plurality of single thin film finishing dies be arranged, export as the plural layers annular membrane by being formed at first annulus between described main body and the described laminate.
The step of described control realizes by following steps, that is: with the temperature of each setting of the described a plurality of single thin film finishing dies of correspondence with compare by the detected temperature of being located on the described single thin film finishing die of at least one temperature sensor; Result based on the comparison, each described a plurality of each cartridge heater of drive, the cartridge heater corresponding with described single thin film finishing die individually heats described single thin film finishing die in a plurality of cartridge heaters that connect described laminate setting to utilize.
The step of described control also has the amount of gas is used in control with step from the described cooling of gas supply pipe supply to cooling, described cooling connects described laminate with gas supply pipe, discharges the cooling gas that is used for each described a plurality of single thin film finishing die cooling.
Each of described a plurality of single thin film finishing dies has upstream side individual layer finishing die and downstream individual layer finishing die, also can form the ring-type path of cool air between described upstream side individual layer finishing die and described downstream individual layer finishing die.The step of described control also has by making from described cooling and flows through described ring-type path of cool air with the described cooling of gas supply pipe with gas, with the be shaped step of cooling of described upstream side individual layer finishing die and described downstream individual layer.
Rack body is located at the bottom of described finishing die and is had cradle portion, and this cradle portion has second annulus that is connected with described first annulus, to export described plural layers.The step of described control realizes by following steps, arrives the film bubble air supply pipe that the airtrapping portion between described rack body and the described laminate that is located at is provided with by connecting described laminate that is:, to described airtrapping portion delivery film bubble gas; The amount of the described film bubble gas that control is supplied with to described airtrapping portion via described film bubble air supply pipe; By connecting gas nozzle that described cradle portion arrives described airtrapping portion to inner described film bubble gas of discharging in the described airtrapping portion from the described plural layers of described second annulus output.
The step of described control also has, and drives at least one the band heater of outer circumferential side be located at described rack body and described finishing die, with the step of the described film bubble gas that heats described airtrapping portion.
The manufacturing process of multilayer blow moulding film also has the step of cooling off described plural layers annular membrane in the downstream of described finishing die.
Described cooling step comprises: carry out the step with air cooled first cooling of described plural layers annular membrane; Carry out cooling off the step of second cooling of described plural layers annular membrane by the ring-type cooling water flow in the downstream of described first cooling body; Carry out cooling off the step of the 3rd cooling of described plural layers annular membrane by the spraying of cooling water in the downstream of described second cooling body.The step of carrying out described first cooling has: supply with described cooling air stream via air supply pipe to described ring-type air blow-off outlet, to be used to cooling air stream from ring-type air blow-off outlet with the air cooled step of described plural layers annular membrane; Regulate the step of the air mass flow of described cooling air stream midway at described air supply pipe; Step at the described cooling air stream of cooling off of described air supply pipe midway.
The step of carrying out described second cooling comprises: the step of supplying with first cooling water via the first cooling water supply pipe; The step of regulating the flow of described first cooling water midway at the described first cooling water supply pipe; The step of cooling off described first cooling water midway at the described first cooling water supply pipe; Described first cooling water is stored to step in the reservoir; Utilization is crossed the weir from described first cooling water of the described reservoir overflow step with described plural layers annular membrane cooling.
The step of carrying out described the 3rd cooling comprises: by on every side spray second cooling water of a plurality of sprayers from described a plurality of film annular membranes, with the step of described plural layers annular membrane cooling; Supply with the step of described second cooling water to described a plurality of sprayers via the second cooling water supply pipe; Step at second cooling water flow of regulating described second cooling water midway of the described second cooling water supply pipe; At the described second cooling water supply pipe midway with the step of described second water quench.
Description of drawings
Fig. 1 is the profile of the internal structure of the existing multilayer blow moulding film shaping machine of expression;
Fig. 2 is the figure of the cooling structure of the existing multilayer blow moulding film shaping machine of expression;
Fig. 3 is the figure of structure of the multilayer blow moulding film shaping machine of expression first embodiment of the invention;
Fig. 4 is the figure that is illustrated in the multilayer blow moulding film shaping machine of first embodiment resin supply pipe group of extending from converter assembly in finishing die;
Fig. 5 is the figure that is illustrated in the section of converter assembly and finishing die in the multilayer blow moulding film shaping machine of first embodiment;
Fig. 6 is the figure that is illustrated in the bottom surface of finishing die in the multilayer blow moulding film shaping machine of first embodiment;
Fig. 7 is the B amplification profile partly of the profile of Fig. 5;
Fig. 8 is the stereogram of the seal that uses in the multilayer blow moulding film shaping machine of first embodiment;
Fig. 9 A is the exploded perspective view of the part of expression single thin film finishing die;
Fig. 9 B is the exploded perspective view of the part of expression single thin film finishing die;
Fig. 9 C is the exploded perspective view of the part of expression single thin film finishing die;
Fig. 9 D is the exploded perspective view of the part of expression single thin film finishing die;
Figure 10 is the top figure of expression downstream individual layer finishing die;
Figure 11 is the front cross-sectional view of expression cooling with the section of gas supply pipe;
Figure 12 is the section plan of expression cooling with the section of gas supply pipe;
Figure 13 is the stereogram of expression cartridge heater;
Figure 14 is the profile of expression film bubble air supply pipe;
Figure 15 is the block diagram of the structure of expression temperature-control circuit;
Figure 16 is the block diagram of structure of cooler of the multilayer blow moulding film shaping machine of expression second embodiment of the invention;
Figure 17 is the profile that the expression air blows out annular nozzle;
Figure 18 is that the expression cooling water flow is down with the profile that encircles;
Figure 19 A is the figure of the existing cooler of expression;
Figure 19 B is the figure of cooler of the multilayer blow moulding film shaping machine of expression second embodiment of the invention;
Figure 19 C is an expression performance curve map relatively.
The specific embodiment
Below, with reference to description of drawings multilayer blow moulding film shaping machine of the present invention.
First embodiment
Fig. 3 is the figure of structure of the multilayer blow moulding film shaping machine of expression first embodiment of the invention.As shown in Figure 3, the multilayer blow moulding film shaping machine of first embodiment has the unit 1 of extrusion and model 2.Extrude unit 1 and have the first extruder 1-1～five extruders of the 5th extruder 1-5 (only representing the first extruder 1-1 and the second extruder 1-2 among Fig. 3).Extrude the position that unit 1 preferably is configured in equal height.
Cooler 6 cools off the coniform film 5 of plural layers, the cylindric film 5 of formation plural layers '.Cooler 6 has: will form that air that the annular barrier air stream of incline direction of the circle-shaped inner face of the coniform film 5 of plural layers blows out blows out function and the taper seat shape of the coniform film 5 of plural layers that keeps extruding from finishing die 4 and with the refrigerating function of coniform film 5 coolings of plural layers.The cylindric film 5 of plural layers ' by 8 flattenings of flattening device.By 8 flattenings of flattening device flat membrane by niproll to 7 the sealing.Niproll has suitable extruder rate to 7.This suitable extruder rate be decision plural layers cylindric film 5 ' the important parameter (design constant) of balance of girth, film thickness, film engineering properties, extrusion mouth diameter that extrudes mouthful with finishing die 4 and the cylindric film 5 of plural layers ' diameter ratio and finishing die 4 extruder rate that extrudes molten resins be directly proportional.Flat plural layers 5 ' in the air capacity of air by the control of the switching value of air capacity control valve 11,11 pairs of air capacities of putting in finishing die 4 from converter assembly 3 of this air capacity control valve are regulated.The wide spoke of warpage that the flat plural layers 5 of flattening " curl flat plural layers 5 by crimping machine 10 " is detected by the wide spoke detector 9 of warpage.
Fig. 4 represents the resin supply pipe group 52 of extending from converter assembly 3 in finishing die 4.Resin supply pipe group 52 has five pipe arrangements of resin supply pipe 52-1～52-5.52-1 is the shortest for the resin supply pipe, and 52-5 is the longest for the resin supply pipe.The resin that injects from extruder 1-1～1-5 supplies to individual layer finishing die in the finishing die 4 via first resin supply pipe 52-1～52-5 respectively.
Fig. 5 represents along the dashdotted converter assembly 3 shown in Figure 4 and the section of finishing die 4.Fig. 7 is the section partial enlarged drawing of finishing die 4.With reference to Fig. 5, be used for five the resin ingress pipe groups 53 (53-1～53-5) be connected that to import from the resin of extruder 1-1～1-5 in the finishing die 4 with converter assembly 3.Resin ingress pipe group 53 is connected respectively with resin supply pipe group 52 in converter assembly 3.Resin ingress pipe 53-1～53-5 is connected with resin supply pipe 52-1～52-5 respectively.
Finishing die 4 has: cylindric model main body 16; Upside model lid 17, it is close to the lower surface of converter assembly 3, and fits tightly with the upper surface of cylindric model main body 16; Downside model lid 18, it is close to the lower surface of cylindric model main body 16.Five single thin film finishing die 19 (19-1～19-5) be disposed at by in cylindric model main body 16, upside model lid 17, downside model lid 18 spaces that form.
Shown in Fig. 5,6, rack body 12 has: outrigger main body 12, and it is close to the lower surface of cylindrical body 16; Medial cradle main body 13, it is close to the lower surface of downside model lid 18.Rack body 12 is close to the lower surface of downside model lid 18, limits the diameter of the firm extrusion coniform film of plural layers afterwards of finishing die 4.
As shown in Figure 5, band heater 67 multistage vertically setting on the outer peripheral face of cylindrical body 16.Band heater 68 is located on the outer peripheral face of outrigger main body 12, especially for heating airtrapping portion 43.Baffle heater 69 is located on upper flange portion top of cylindrical body 16.Like this, finishing die 4 roughly heats from its whole outer peripheral face, makes inner body keep roughly even temperature.In addition, a plurality of cartridge heaters 71 form as bar-shaped calandria, are configured to connect vertically finishing die 4.About airtrapping portion 43 and cartridge heater 71 aftermentioneds.
Single thin film finishing die 19-1～19-5 is multistage vertically overlapping, forms the laminate of single thin film finishing die.Fig. 9 A～Fig. 9 D is the exploded perspective view of each single thin film finishing die.With reference to Fig. 9 A～9D, the s single thin film finishing die 19-s among single thin film finishing die 19-1～19-5 has ring-type insulator 22, upstream side individual layer finishing die 19-sU, air seal ring 23, sealing ring 24, downstream individual layer multilevel shaping mould 19-sD.Each of upstream side individual layer finishing die 19-sU and downstream individual layer finishing die 19-sD has frustoconical platform shape, forms and the similar recess of truncated cone shape in the bottom.Ring-type insulator 22 and the coaxial mounting of upstream side individual layer finishing die 19-sU are on the central portion of upstream side individual layer finishing die 19-sU.On ring-type insulator 22, be provided with the hole, wherein connect five resin supply pipe 52-1～52-5 that the single thin film finishing die 19-1～19-5 that is used for to five rank imports resin.On the recess of upstream side individual layer finishing die 19-sU top, on the top of the chimeric upstream side individual layer of the recess finishing die 19-(s+1) of downstream individual layer finishing die 19-sD U by air seal ring 23 and sealing ring 24 chimeric downstream individual layer finishing die 19-sD.Work as ring-type path of cool air 59 (aftermentioned) in upstream side individual layer finishing die 19-sU that is limited by air seal ring 23 and sealing ring 24 and the space between the individual layer finishing die 19-sD of downstream.In addition, on upstream side individual layer finishing die 19-sU, be formed with eight holes that resin supply pipe 52-1～52-5 uses.In eight holes, five holes are corresponding with the hole on being formed at ring-type insulator 22.In addition, concerning the through hole that is used for the resin supply pipe, what do not need to connect does not then offer.
Upstream side individual layer finishing die 19-s is connected with resin supply pipe 52-s by the connecting hole of being located on the upstream side individual layer finishing die 19-sU.As shown in Figure 7, molten resin stream 54-sU extends to the axle center in the bottom of upstream side individual layer finishing die 19-sU, and from then on extends downwards from this connecting hole longitudinal extension.Downstream individual layer finishing die 19-sD has connecting hole at central part, engages the molten resin stream 54-sU that extends from upstream side individual layer finishing die 19-sU on this connecting hole.Downstream individual layer finishing die 19-sD is connected with its connecting hole, has eight molten resin stream 55-sD that extend along radial direction.The relative end of each molten resin stream 55-sD is open in the circular cone side of downstream individual layer finishing die 19-sD.This end with on taper seat, be connected while rotating the spiral flow path 56-sD that advances vertically.Figure 10 is the top figure of downstream individual layer finishing die 19-sD and cylindric model main body 16, also represents molten resin stream 54-sU.Spiral resin flow stream 57-sD is formed by the side and the spiral flow path 56-sD of upstream side individual layer finishing die 19-sU bottom.Spiral resin flow stream 57-sD has towards the composition in downstream with towards the composition of circumferencial direction, extends the tangential direction 58 of the circle on the axle right-angle plane roughly in the position, outer end toward the outer side towards the downstream and gently.Each outboard end of a plurality of spiral resin flow stream 57-sD is connected with the annular gap 41 that is formed between multilevel shaping mould and cylindric model main body 16 inner faces.Spiral flow forms stream 57-sD and forms thin more shallowly more by the downstream more.
Shown in Fig. 9 B, upstream side individual layer finishing die 19-sU has smooth frustoconical face.The frustoconical face of upstream side individual layer finishing die 19-1U is connected across the bottom surface of ring-type insulator 22 with upside model lid 17.Below the side of upstream side individual layer finishing die 19-sU, be formed with step.
The periphery of the upper cone table top of downstream individual layer finishing die 19-sD has the projection of extending towards the top.Thus, the central portion of the upper cone table top of downstream individual layer finishing die 19-sD forms depressed part.The periphery of portion also is formed with groove in the central.Equally, on upstream side individual layer finishing die 19-sU, on the recess that forms from the bottom, and formation depressed part corresponding with the depressed part of the central portion of the upper cone table top of downstream individual layer finishing die 19-sD.Configuration air seal ring 23 between upstream side individual layer finishing die 19-sU and downstream individual layer finishing die 19-sD makes the outer circumferential side of the depressed part of itself and upstream side individual layer finishing die 19-sU and downstream individual layer finishing die 19-sD be adjacent to chimeric.In addition, the interior all sides at depressed part dispose sealing ring 24.Thus, form ring-type cooling air flow circuit 59 by depressed part, air seal ring 23 and sealing ring 24.Stop air to flow or opposite flowing by air seal ring 23 and sealing ring 24 from the zone between export-oriented upstream side individual layer finishing die 19-sU of single thin film finishing die 19-s and the downstream individual layer finishing die 10-sD.In addition, flow at ring-type cooling air flow circuit 59 by making the cooling air, single thin film finishing die 19-s can be cooled off equably.
Lower end at downstream individual layer finishing die 19-sD is formed with recess with the level.Like this, the sealing ring 35 of allocation plan 8 makes the step of the recess of itself and downstream individual layer finishing die 19-sD lower end and below, upstream side individual layer finishing die 19-(s+1) U side chimeric.As shown in Figure 7, sealing ring 35 suppresses the heat conduction between downstream individual layer finishing die 19-sD and upstream side individual layer finishing die 19-(s+1) U, and prevents that resin flow from flowing between them.
As shown in figure 13, cartridge heater 71 with connect the heater mounting hole 74U of single thin film finishing die 19-sU vertically and connect the heater mounting hole 74D of downstream individual layer finishing die 19-sD vertically chimeric.Such cartridge heater 71 is configured on the circumference symmetrically at finishing die 4 axis centers.Also can be configured on the concentric circles.Cartridge heater 71 has good pyroconductivity, hear resistance and electrical insulating property, and has Heating tube at the height and position corresponding with the plural layers finishing die 19-s that is predetermined.This Heating tube is generated heat by the electric lead supply capability in the cartridge heater 71, and single thin film finishing die 19-s is heated.Like this, cartridge heater 71 relative each a plurality of single thin film finishing die 19-s are provided with, and can individually heat single thin film finishing die 19-s.
As shown in figure 10, a plurality of radiation directions stream of downstream individual layer finishing die 19-sD form stream 55-s near dispose to detect and flow to the temperature sensor 75-s of temperature that radiation direction stream forms the resin flow of stream 55-s.In this embodiment, corresponding with a downstream individual layer finishing die 19-sD, dispose a temperature sensor 75-s.But also a plurality of temperature sensors can be set.
As shown in Figure 7, limit ring-type path of cool air 59 by air seal ring 23 and sealing ring 24.Figure 11 and Figure 12 represent cooling gas supply pipe 76.Cooling is the dual pipes that formed by outer tube 77 and interior pipe 78 with gas supply pipe 76.In interior pipe 78, a pair of projection 79 shown in Figure 12 forms vertically continuously, is divided into air donor site and air between outer tube 77 and the interior pipe 78 and discharges two parts in position.Offer air introducing port 80I that imports to the air donor site and the air outlet 800 that is communicated with air discharge position at outer tube 77.With corresponding with the single thin film finishing die 19-s on each rank and be set in height on the outer tube 77 especially, on outer tube 77, offer to ring-type path of cool air 59 and import the air introducing port 80I of cooling air and discharge the air outlet 800 of cooling air from ring-type path of cool air 59.In the present embodiment, this cooling connects multistage single thin film finishing die 19 and is provided with one with gas supply pipe 76.As shown in Figure 5, in supply road, be provided with switch valve 85 and choke valve 86 with tempering air 84 air supply introducing port 80I.Distance between the datum level of the air introducing port 80I on each rank or air outlet 800 and upside model lid 17 is represented by a+ (s-1) b.Here, a is a constant, and b is the single thin film finishing die 19-s of adjacency up and down, and the axial flow of s-1 is to leaving distance.Flow-rate adjustment choke valve 86 preferably is set between switch valve 85 and air introducing port 80I.When the temperature of different types of resin independently is set, a plurality of coolings gas supply pipe 76 is set preferably.Can control the add temperature of Flow-rate adjustment respectively by every rank with the throttling degree of choke valve 86 and the heater 71 stated.
With reference to Fig. 5, relatively outrigger main body 12 and medial cradle main body 13 support 37 that is embedded into their lower surface side forms the part of the delivery port of having stated.The part of the annular gap 42 that links to each other with annular gap 41 is formed in the support.As shown in Figure 5, support 37 is formed by interior side ring 37-1 and outer ring 37-2.The part of annular gap 42 forms as the gap between interior side ring 37-1 and the outer ring 37-2.Interior side ring 37-1 is by the position of adjusting its radial directions towards the first axial adjustment bolt 38, and outer ring 37-2 is by adjusting the position that bolt 39 is adjusted its radial directions towards second of radial direction.Position by support 37 is adjusted, and can adjust the thickness of the coniform film 5 of plural layers.Heat controller (not shown) receives the thickness signal that thickness meter that thickness to the cylindric film 5 of the plural layers ' flat plural layers 12 after solidifying that are cooled carries out instrumentation is exported, and this heat controller carries out the temperature control of support 37 by heater 68 and 69.The gap that the control second molten resin multilayer film forms the holder part of annular gap 25 is shunk in the expansion that is carried out temperature controlled support 37.
As shown in Figure 5, medial cradle main body 13 is fixed on the downside model by axial bolts 45 and covers.In the lower surface side of downside model lid 18, between downside model lid 18 and medial cradle main body 13, be formed with airtrapping portion 43.Gas nozzle 36 connects medial cradle main body 13 and installs.Gas nozzle 36 is blown into air with the pressure air in the airtrapping portion 43 in the inner space of the coniform film 5 of the lower surface of medial cradle main body 13 side direction plural layers.The lower end opening port of film bubble air supply pipe 47 is open in airtrapping portion 43.Disturb plate 49 in airtrapping portion 43, to enlarge symmetrically along centrifugal direction and axial line.Disturb plate 49 to have the heat effect that film bubble air that the static pressure that can not produce dynamic pressure at the inboard open end of gas nozzle 36 turns usefulness into and will be discharged to the coniform film of plural layers 5 inner spaces is brought up to the temperature of the coniform film 5 of plural layers that extrudes from annular gap 42.
With reference to Figure 14, the annulus 92 that films bubble in the importing airtrapping portion 43 passes through between outer tube 94 and the interior pipe 93 from the hole 95 that is opened on the downside model lid 18 with air is also discharged by choke valve (not shown) throttling of being located in the discharge pipe via the outlet 89 that is opened on the outer tube 94.If the cylindric film 5 of plural layers ' diameter reduce, then regulate air pressures by air pressure control valve 97, the switch valve 98 that is disposed at air pressure control valve 97 downstreams is opened, increase the air capacity in the film bubble.
With reference to Fig. 5, the annular gap 41 between the cylinder outer peripheral face of the laminate of single thin film finishing die 19 and the cylinder inner peripheral surface of cylindrical body 16 limits the suitable outside dimension of the coniform film 5 of plural layers and suitable wall thickness.The suitable outside dimension of annular gap 42 these multilayered molten resin films of qualification between the inner peripheral surface of the outer peripheral face of medial cradle main body 13 and outrigger main body 12 and the suitable wall thickness and the suitable discharge angle of multilayered molten resin film.The annular gap 41 of upstream side is connected continuously with the annular gap 42 in downstream.Annular gap 42 constitutes towards the downstream undergaugeization or hole enlargementization (being undergaugeization in the illustrated example) continuously, and adjustment is from the delivery port of the diameter of the coniform film 5 of plural layers of outrigger main body 12 extrusion.
Figure 15 represents control circuit 100.Control circuit 100 is controlled to cooling gas supply pipe 76 gas supplied amounts by gauge tap valve 85 and choke valve 86, waits by control air pressure control valve 97 and switch valve 98 and controls the gas flow of supply to film bubble air supply pipe 47.Thus, cool off with the laminate of gas by cooling single thin film finishing die 19-s.In addition, control circuit 100 control band heaters 67,68,69, heating finishing die 4.In addition, control circuit 100 has temperature control part 62, and temperature control part 62 is individually controlled the temperature of each single thin film finishing die 19-s of laminate.Therefore, temperature control part 62 relative each single thin film finishing die 19-s have target temperature setting apparatus 31-s, comparison control part 32-s, output circuit 33-s.Relatively control part 32-s will be compared by the temperature sensor 75-s that is located on the single thin film finishing die 19-s temperature that obtains and the temperature that is set in the temperature setting device 31-s, and comparative result is outputed in the output circuit 33-s.Output circuit 33-s result based on the comparison drives cartridge heater 71-s, heating single thin film finishing die 19-s.Owing to use gas touring in ring-type path of cool air 59 from the cooling that cooling is discharged with gas supply pipe 76, so single thin film finishing die 19-s is cooled to below the design temperature.Temperature control part 62 is heated to design temperature by driving the cartridge heater 71-s of each single thin film finishing die 19-s setting relatively with each single thin film finishing die 19-s.Like this, the forming temperature of control resin film.
The first kind of molten resin that is directed in the resin ingress pipe 53-1 is directed to resin supply pipe 52-1, molten resin stream 54-1U by upstream side individual layer finishing die 19-1U, send into the connecting hole of downstream individual layer finishing die 19-1D, and distribute to a plurality of spiral resin stream 57-1D via molten resin stream 55-1D.Like this, first kind of molten resin tangentially is forced in the annular gap 41.Second kind of molten resin is directed to resin supply pipe 52-2, molten resin stream 54-2U by upstream side individual layer finishing die 19-2U, send into the connecting hole of downstream individual layer finishing die 19-2D, and distribute to a plurality of spiral resin flow stream 57-2D via molten resin stream 55-2D.Like this, second kind of molten resin tangentially is forced in the annular gap 41.The third molten resin is directed to resin supply pipe 52-3, molten resin stream 54-3U by upstream side individual layer finishing die 19-3U, send into the connecting hole of downstream individual layer finishing die 19-3D, and distribute to a plurality of spiral resin flow stream 57-3D via molten resin stream 55-3D.Like this, the third molten resin tangentially is forced in the annular gap 41.The 4th kind of molten resin is directed to resin supply pipe 52-4, molten resin stream 54-4U by upstream side individual layer finishing die 19-4U, send into the connecting hole of downstream individual layer finishing die 19-4D, and distribute to a plurality of spiral resin stream 57-4D via molten resin stream 55-4D.Like this, the 4th kind of molten resin tangentially is forced in the annular gap 41.The 5th kind of molten resin is directed to resin supply pipe 52-5, molten resin stream 54-5U by upstream side individual layer finishing die 19-5U, send into the connecting hole of downstream individual layer finishing die 19-5D, and distribute to a plurality of spiral resin flow stream 57-5D via molten resin stream 55-5D.Like this, the 5th kind of molten resin tangentially is forced in the annular gap 41.
As shown in Figure 5, the resin supply pipe 52-ss different mutually by length supply with different molten resins to single thin film finishing die 19-s respectively, and its spiral resin flow stream 57-sD from the differing heights position is forced in the annular gap 41.Before different resins arrives annular gap 41, not with different mixed with resin.Be forced into annular gap 41 and the medial surface of the first cylindric resin film that forms at spiral resin flow stream 57-1D from first height and position, second resin that tangentially extrudes from the spiral resin flow stream 57-2D of second height and position does not mix with the first cylindric resin film, and engage as the inner face side of second rank with the first cylindric resin film, form the second cylindric resin molding.The 3rd resin that tangentially extrudes from the spiral resin flow stream 57-3D of the 3rd height and position does not mix with the second cylindric resin film, and form the 3rd cylindric resin molding in the inner face side of the second cylindric resin film, the 4th resin that tangentially extrudes from the spiral resin flow stream 57-4D of the 4th height and position does not mix with the 3rd cylindric resin film, and form the 4th cylindric resin molding in the inner face side of the 3rd cylindric resin film, the 5th resin that tangentially extrudes from the spiral resin flow stream 57-5D of the 5th height and position does not mix with the 4th cylindric resin film, and forms the 5th cylindric resin molding in the inner face side of the 4th cylindric resin film.The coniform film 5 of plural layers is discharged from the holder part of annular gap 42 as the five b stage resin b films that form like this.Import film bubble air from gas nozzle 36 to the inner space of the coniform film 5 of such plural layers, the coniform film 5 of these plural layers is held as being defined the expander of diameter.This expander is in the hole enlargement effect that is subjected to continuously towards cooler 6 midway, further by filming.The width of the cylindric film 5 of plural layers that extrudes from the cradle portion of annular gap 42 is adjusted by air capacity and its pressure of the film bubble air of discharging from film bubble air supply pipe 47.
Upside model the lid 17 and first rank single thin film finishing die 19-1 also can be used as the one thing and forms.Downside model lid the 18 and the 5th rank single thin film finishing die 19-5 also can be used as the one thing and forms.The integrated model structure of finishing die 4 can the simplification like this can reduce the assembling procedure number.In the structure of having stated, the first rank single thin film finishing die 19-1 is configured in upside, the 5th rank single thin film finishing die 19-5 is configured in downside, but also upstream side and downstream along continuous straight runs can be disposed, and can organize the structure that changes into the coniform film 5 along continuous straight runs extrusion of plural layers.
Distance between the downstream openend of the molten resin stream 54-sU of the resin supply pipe 52-s of the quantity of corresponding exponent number and the reference position is represented with the identical formula of the described numerical expression of the tempering air introducing port 80I of gas supply pipe 76 and the distance between the reference position by the expression cooling.Film bubble air supply pipe 47 and cooling connect in the finishing die 4 with gas supply pipe 76, twist solid by the bolt at two ends.Like this, the single thin film finishing die 19 of multistage laminate is fixing vertically, constitutes integratedly, structurally is stable.Solid and integrated by upside model lid 17 and cylindric model main body 16 bolts are twisted, with cylindric model main body 16 and medial cradle main body 13 and outrigger main body 12 bolts twist solid and integrated, with gas supply pipe 76 multiple-rank arrangement of single thin film finishing die 19-s is merged with one heart integratedly by film bubble air supply pipe 47 and cooling, make model 4 single structureizations.In this single structure body,, can improve the quality of multilevel shaping film by single thin film finishing die 19 being controlled to be suitable temperature by every rank.Consequently, multilayer blow moulding film shaping machine of the present invention and plural layers manufacturing process are regarded the multiple-rank arrangement model as single temperature control volume and are realized its unified temperature is controlled.
Second embodiment
Putting into the air capacity of the air 90 in the finishing die 4 is controlled by the switch of air capacity control valve 98.Supplying with control that road 47 imports the air capacity of finishing dies 4 inboards via air is that the expansion ratio as the hole enlargement degree of finishing die 4 is controlled.Flattening film 5 " the warpage wide cut detect by warpage wide cut sensor 9.
Figure 16 is illustrated in when keeping film bubble shape, with the cooler 6 of the cylindric film 5 of plural layers ' cooling in detail.Cooler 6 has the cooling body that carries out the cooling of three stages.This cooling body has first cooling body 117, second cooling body 118, the 3rd cooling body 119.In addition, be provided with radiation thermometer 191 and 192.Radiation thermometer 191 is located at the upstream side of first cooling body 117, and radiation thermometer 192 is located at the upstream side of second cooling body 118 in the downstream of first cooling body 117.
First cooling body 117 have annularly to plural layers cylindrical thin-film 5 ' the cylindrical portions may gas sparge ring 121 and the gas delivery volume mechanism 122 of spraying tempering air.On gas sparge ring 121, offer medium pore 123.Plural layers cylindrical thin-film 5 ' cylindrical portions may near the medium pore 123 of gas sparge ring 121, push downwards and hang down.Side periphery is provided with air and blows out annular nozzle 124 on the medium pore of gas sparge ring 121.Air blows out annular nozzle 124 and forms as shown in figure 17.Blowing out ring-type cooling air stream that annular nozzle 124 blows out from air has to the composition at center and the composition that makes progress and towards oblique upper.The downside circular opening 126 that air blows out annular nozzle 124 is open in gas sparge ring 121, upside circular opening 127 towards the cylindric film 5 of plural layers ' cylindrical portions may, open in gas sparge ring 121 outsides.
As shown in figure 16, the downstream end face of finishing die 4 is restricted to altitude datum position 128.The distance of the short transverse between the upside circular opening 127 of altitude datum position 128 and gas sparge ring 121 is set at h1.The height and position of gas sparge ring 121 can be adjusted by upper-lower position adjusting device (not shown).The upper-lower position adjusting device has to be adjusted the rotary screw of axial height and twists and close on this rotary screw and be fixed on the nut combinations on the gas sparge ring 121 and the known linear feed mechanism that obtains multilayer blow moulding film shaping machine main body being used for.The distance h 1 of short transverse is carried out the position adjustment by upper-lower position adjusting device as described above.
The air supply pipe road 131 that gas delivery volume controlling organization 122 contains air blast 129, air blast is connected with gas sparge ring 121.In air supply pipe road 131, be provided with the controllable register 132 and first heat exchanger 133 of regulating supply flow rate.First heat exchanger 133 will be cooled to proper temperature from the air that air blast 129 is sent.Be provided with air pressure probe 134 and air temperature sensor 135 in the air supply pipe road 131 between first heat exchanger 133 and gas sparge ring 121.Air pressure probe 134 detects the pressure that imports to the air in the gas sparge ring 121, and air temperature sensor 135 detects the temperature that imports to the air in the gas sparge ring 121.
By radiation thermometer 191 measure plural layers cylindrical thin-films 5 ' temperature, if measure temperature than the target temperature height of setting, then control to adjust baffle plate 132, cooling air delivery is increased, if design temperature is lower than the target temperature of setting, then control to adjust baffle plate 132, cooling air stream flow is reduced.
The first cooling water quantity delivered mechanism 136 has first water pump 145 and first water pump 145 is supplied with water route 146 with first cooling water that ring 160 is connected down with cooling water flow.Supply with the first flow control valve 147 and second heat exchanger 148 that is provided with the adjusting supply water yield in the water route 146 at first cooling water.The water quench that second heat exchanger 148 will be sent from first water pump 145 is to proper temperature.Under first flow control valve 147 and cooling water flow, supply with in the water route 146 and be provided with first cooling-water temperature sensor 149 with first cooling water of ring between 160.First cooling-water temperature sensor 149 detects and imports under the cooling water flow with the temperature of encircling first cooling water in 160.
By radiation thermometer 192 measure plural layers cylindrical thin-films 5 ' temperature, if measure temperature than the target temperature height of setting, then control first flow control valve 147, cooling water flow is increased, if design temperature is lower than the target temperature of setting, then control first flow control valve 147, cooling water flow is reduced.
Like this, in the present embodiment, using has two radiation thermometers 191 and 192, but also can use one of them.In this case, use the control of radiation thermometer.
In addition, dehydrator 151 dewaters, to remove moisture as much as possible.This be because, when having the moisture of the alternating temperature that when cooling use, even the spraying cooling water, cooling effectiveness also can worsen.The water that is excluded is not merely drained, but is stored in the cistern (not shown).The water of this cistern uses in ensuing the 3rd cooling body 119.Can apply flexibly resource effectively like this, and also can reduce cost.
The 3rd cooling body 119 has the cooling water dispenser group 152 and the second cooling water quantity delivered mechanism 153.A plurality of cooling water sprayer jet pipes 154 of cooling water dispenser group 152, with the cylindric film 5 of plural layers ' cylindrical portions may be that the center disposes radially.Front end position separately at a plurality of cooling water sprayer jet pipes 154 is separately installed with cooling water discharge nozzle 155 convertibly.Cooling water sprayer jet pipe 154 disposes regularly and is bearing on the shared support ring 157.Distribute loop pipe 158 to supply with to a plurality of cooling water sprayer jet pipes 154 distributively from the cooling water that is fixed on the shared support ring 157 cooling water.
The second cooling water quantity delivered mechanism 153 has second water pump 159 and supplies with water route 161 with second cooling water that distributes loop pipe 158 to be connected second water pump 159 and cooling water.Supply with second flow control valve 162 and the 3rd heat exchanger 163 that is provided with the adjusting supply water yield in the water route 161 at second cooling water.The water quench that the 3rd heat exchanger 163 will be sent from second water pump 159 is to proper temperature.Second cooling water between the 3rd heat exchanger 163 and cooling water distribution loop pipe 158 is supplied with in the water route 161 and is provided with the cooling pressure sensor 164 and second cooling-water temperature sensor 170.Cooling water pressure sensor 164 detects and imports to the pressure that cooling water distributes second cooling water of loop pipe 158, and second cooling-water temperature sensor 170 detects and imports to the temperature that cooling water distributes second cooling water in the loop pipe 158.
Height gage between the centre of dispersion line of dehydrator 151 and cooling water discharge nozzle 155 is decided to be h4.Height h4 carries out the position adjustment by the 3rd upper-lower position adjusting device of the structure identical with the first upper-lower position adjusting device of having stated.
Figure 19 A～Figure 19 C represents the test example that multilayer blow moulding of the present invention is film shaped.Figure 19 C be the cylindric film 5 of plural layers in three mutually different cooling means of expression ' the travel distance of cylindrical portions may reduce the curve map that concerns with temperature.Figure 19 C represents the contrast of three stages of the present invention cooling with the two-stage cooling device 203,204 of equipment 121,160,154 and the existing apparatus stated.The cylindric film 5 of plural layers of the cooling of first temperature curve 166 expression in the curve map by three stages cooling of the present invention (gas cooled, water cooling, drip washing cooling) ' the outer field temperature of resin of cylindrical portions may reduce.The cylindric film 5 of plural layers of second temperature curve 167 expression cooling by three stages cooling of the present invention ' the temperature of resin internal layer of cylindrical portions may reduce, the cylindric film 5 of plural layers of the 3rd temperature curve 168 expression cooling by the two-stage cooling (gas cooled and water cooling) of prior art ' the outer field temperature of resin of cylindrical portions may reduce, the cylindric film 5 of plural layers of the 4th temperature curve 169 expressions cooling by this two-stage cooling ' the temperature of resin internal layer of cylindrical portions may reduce.The multi-layer resinous cylindric film 5 of the 5th temperature curve 171 expression cooling by the stage cooling (only gas cooled) of prior art ' the outer field temperature of resin reduce, the multi-layer resinous cylindric film 5 of the 6th temperature curve 172 expressions cooling by the stage cooling of prior art ' the temperature of resin internal layer reduce.
The cooling multi-layer cylinder shape film in, lower resin crystallization temperature Tc2 the layer more in the inner part, higher resin crystallization temperature Tc1 the layer more in the outer part.Forming under the situation of ectonexine by resin crystallization temperature Tc1, material that Tc2 is low, in existing two-stage cooling means, can not be in short interval intercrystallineization, the low time of temperature is longer, and this crystallization suppresses not enough.
Air in three stages of the present invention cooling blows out in first section cooling that annular nozzle 124 carries out, from air blow out cooling air that annular nozzle 124 blows out with respect to the cylindric film 5 of plural layers ' the mobile reverse flow of cylindrical portions may, compare with the forward stream cooling of existing cooling, the gradient of chilling temperature is big especially, improves the cooling effectiveness of first section cooling significantly.Utilize such adverse current cooling, skin is cooled near the crystallized temperature Tc1 in the outside.The water cooling of second cooling afterwards is cooled to the low temperature than outer field crystallized temperature Tc1 rapidly with skin.Rapid cooling like this realizes the curing of the state that the crystallization rate is low.In this solidification process, plural layers cylindrical thin-film 5 ' intermediate layer and internal layer be cooled near separately the crystallized temperature.Secondly, finish the dehydrated device 151 of current film of heat exchange and remove.And then the water cooling of the 3rd cooling afterwards is cooled to its crystallized temperature Tc2 rapidly with inner layer resin.
Rapid cooling like this, the particularly rapid cooling of second cooling can promote the curing of the state that the crystallization rate is low, suppress the development of inner deformational stress, and can suppress the generation of curling of the inflation film of end article.In addition, can guarantee its transparency well.High efficiency cooling like this realizes by the distance that shortens between the cooling zone of being represented by the longitudinal axis of the curve map of Figure 19 C.The vertical direction size of the cooling system of configuration device realizes this shorteningization by dwindling longitudinally, and such result who dwindles has subdued the cost of equipment of device.
In each of three cooling stages, with the temperature optimization that lowers efficiency.By controllable register 132 control air quantity with by first heat exchanger, 133 control cooling capacities, make the maximization of first cooling effectiveness.The excessive increase of increase that air quantity is excessive and heat exchange amount makes operating cost excessive.The cooling capacity of necessary degree reduces operating cost.So adjust the drop distance h 1 of short transverse, make minimizing of its operating cost.By the first flow control valve 147 control water yields with by second heat exchanger, 148 control cooling water capacities, make the maximization of second cooling effectiveness.The excessive increase of increase that the water yield is excessive and heat exchange amount makes operating cost excessive.The cooling capacity of necessary degree reduces operating cost.So regulate the drop distance h 2 of short transverse, make minimizing of its operating cost.By second flow control valve, the 162 control water yields, by the 3rd heat exchanger 163 control cooling water capacities, make the maximization of the 3rd cooling effectiveness.The excessive increase of increase that the water yield is excessive and heat exchange amount makes operating cost excessive.The cooling capacity of necessary degree reduces operating cost.So adjust the drop distance h 3 of short transverse, make minimizing of its operating cost.
The following realization of such optimized running, based on by air pressure probe 134, air temperature sensor 135, first cooling-water temperature sensor 149, cooling water pressure sensor 164, the detection signal of second cooling-water temperature sensor, 170 detected pressure and temperatures, control air supply pipe road 131, first flow control valve 147, the aperture separately of second flow control valve 162, the heat-exchange capacity separately (flow of cold-producing medium) of first heat exchanger 133 and second heat exchanger 148 and the 3rd heat exchanger 163, be equivalent to the cylindric film 5 of plural layers ' the initial cooling zone of cylindrical portions may between the distance h 1 of length, the distance h 2 that is equivalent to the height of the water surface 141 corresponding to spillway discharge, the distance h 3 that overflow flows down, the distance h 4 corresponding with distribution.
Multilayer blow moulding film shaping machine of the present invention and the film shaped method of multilayer blow moulding are cured by suppressing crystallization, can improve the quality of end article.
Claims (28)
1, a kind of multilayer blow moulding film shaping machine is characterized in that having: converter, and it is used to supply with various kinds of resin; Finishing die, it is located at the axial downstream of described converter; Temperature control device,
Described multiple molten resin is individually supplied with to described finishing die via described converter,
Described finishing die has: main body; The laminate of a plurality of single thin film finishing dies, described a plurality of single thin film finishing dies along described axial arrangement, generate the film of described resin corresponding in the described multiple molten resin in the inside of described main body; First annulus, it is formed between described main body and the described laminate,
Lamination has the plural layers of a plurality of described films to export as the plural layers annular membrane by described first annulus,
Described temperature control device is independently controlled the temperature separately of described a plurality of single thin film finishing dies.
2, multilayer blow moulding film shaping machine as claimed in claim 1 is characterized in that, described temperature control device has: a plurality of cartridge heaters, and it connects described laminate and is provided with; At least one temperature sensor, it is located on each of described a plurality of single thin film finishing dies of described laminate; Control circuit, it heats single thin film finishing die corresponding in described a plurality of single thin film finishing die based on by the temperature of each described a plurality of single thin film finishing dies settings relatively with by the described a plurality of cartridge heaters of the detected temperature difference drive of described temperature sensor respectively separately to utilize described a plurality of cartridge heater.
3, multilayer blow moulding film shaping machine as claimed in claim 2, it is characterized in that, described temperature control device also has the cooling gas supply pipe, this gas supply pipe connects described laminate setting, discharge is used for the cooling gas with each cooling of described a plurality of single thin film finishing dies, the described cooling that described control circuit control is supplied with gas supply pipe to the described cooling amount of gas.
4, multilayer blow moulding film shaping machine as claimed in claim 3, it is characterized in that, each of described a plurality of single thin film finishing dies has upstream side individual layer finishing die and downstream individual layer finishing die, between described upstream side individual layer finishing die and described downstream individual layer finishing die, form the ring-type path of cool air, flow through described ring-type path of cool air with the described cooling of gas supply pipe with gas by making from described cooling, thereby with described upstream side individual layer finishing die and the cooling of downstream individual layer finishing die.
5, as each described multilayer blow moulding film shaping machine in the claim 1～4, it is characterized in that also having rack body, it is located at the bottom of described finishing die and has cradle portion, this cradle portion has second annulus that is connected with described first annulus, to export described plural layers
Described temperature control device has: airtrapping portion, and it is located between described rack body and the described laminate; Film bubble air supply pipe, it connects described laminate and arrives described airtrapping portion, is used for the delivery film bubble gas to described airtrapping portion; Gas nozzle, it connects described cradle portion and arrives described airtrapping portion, the described film bubble gas to discharge described airtrapping portion from the inside of the described plural layers of described second annulus output in,
The amount of the described film bubble gas that the control of described control circuit is supplied with to described airtrapping portion via described film bubble air supply pipe.
6, multilayer blow moulding film shaping machine as claimed in claim 5, it is characterized in that, described temperature control device also has the band heater of at least one side's who is located at described rack body and described finishing die outer peripheral face, described control circuit drives described band heater, to heat the described film bubble gas in the described airtrapping portion.
7, as each described multilayer blow moulding film shaping machine in the claim 1～4, it is characterized in that also having cooling body, this cooling body is located at the downstream of described finishing die, is used to cool off described plural layers annular membrane.
8, multilayer blow moulding film shaping machine as claimed in claim 7 is characterized in that, described cooling body has: first cooling body, and it cools off described plural layers annular membrane by the cooling air; Second cooling body, it is located at the downstream of described first cooling body, by the ring-type cooling water flow described plural layers annular membrane is cooled off; The 3rd cooling body, it is located at the downstream of described second cooling body, by the spraying of cooling water described plural layers annular membrane is cooled off.
9, multilayer blow moulding film shaping machine as claimed in claim 8, it is characterized in that, described cooling body also has first radiation thermometer of noncontact mensuration from the temperature of the described plural layers annular membrane of described finishing die output, and described first cooling body is controlled the flow of described cooling air based on the temperature of being measured by described first radiation thermometer.
10, multilayer blow moulding film shaping machine as claimed in claim 8, it is characterized in that, described first cooling body has: air supply pipe, it supplies with cooling air stream to ring-type air blow-off outlet, to flow by the described cooling air from described ring-type air blow-off outlet described plural layers annular membrane air cooling; Air regulator, it is located in the described air supply pipe, regulates the air mass flow of described cooling air; Heat exchanger is used in the air cooling, and it is located in the described air supply pipe, cools off described air.
11, multilayer blow moulding film shaping machine as claimed in claim 8, it is characterized in that, described cooling body also has second radiation thermometer of noncontact mensuration from the temperature of the described plural layers annular membrane of described first cooling body output, and described second cooling body is controlled the flow of described ring-type cooling water flow based on the temperature of being measured by described second radiation thermometer.
12, multilayer blow moulding film shaping machine as claimed in claim 8 is characterized in that, described second cooling body has: the first cooling water supply pipe, and it supplies with first cooling water; The first cooling water flow adjuster, it is located in the described first cooling water supply pipe, regulates the flow of described first cooling water; The first cooling water heat exchanger, it is located in the described first cooling water supply pipe, cools off described first cooling water; Reservoir, it stores described first cooling water,
Described reservoir has the weir, and it is located at the inboard top of described reservoir, can adjust apart from the height of the water surface of described first cooling water, so that described first cooling water is as the overflow of described ring-type cooling water flow.
13, multilayer blow moulding film shaping machine as claimed in claim 8, it is characterized in that, described cooling body also has and is used to remove the dehydrator that is attached to the moisture from the described plural layers annular membrane of described second cooling body output, and the distance of described second cooling body and described dehydrator is adjustable.
14, multilayer blow moulding film shaping machine as claimed in claim 8 is characterized in that, described the 3rd cooling body has: a plurality of sprayers, its be located at described plural layers annular membrane around, second cooling water of spraying; The second cooling water supply pipe, it supplies with described second cooling water to described a plurality of sprayers; The second cooling water flow adjuster, it is located in the described second cooling water supply pipe, regulates second cooling water flow of described second cooling water; The second cooling water heat exchanger, it is located in the described second cooling water supply pipe, cools off described second cooling water.
15, multilayer blow moulding film shaping machine as claimed in claim 1, it is characterized in that, described a plurality of single thin film finishing die has same size, each of described a plurality of single thin film shaping dies has the upstream side individual layer finishing die of truncated cone shape and engages the downstream individual layer finishing die of the truncated cone shape that also combines in the downstream with described upstream side individual layer finishing die
Described upstream side individual layer finishing die and described downstream individual layer finishing die have recess in the bottom, the described recess of described downstream individual layer finishing die and described upstream side individual layer finishing die is chimeric, described upstream side individual layer finishing die is accepted described resin corresponding in the described multiple molten resin, supply with to described downstream individual layer finishing die
The helical form resin passage that described downstream individual layer finishing die has radial resin passage and the side that is formed at the described frustum of a cone and is connected with described radial resin passage will output to described first annulus from the described resin of described upstream side individual layer finishing die via described radial resin passage and described helical form resin passage.
16, the film shaped method of a kind of multilayer blow moulding is characterized in that, has following step:
The temperature of each of a plurality of single thin film finishing dies of independent control;
Finishing die has main body and at the laminate of described body interior along described a plurality of single thin film finishing dies of described axial arrangement, by converter multiple molten resin is supplied with to described a plurality of single thin film finishing dies respectively;
Generate the film of described resin corresponding in the multiple molten resin by each of described a plurality of described single thin film finishing dies;
Make lamination plural layers from the described film of described a plurality of single thin film finishing dies be arranged, export as the plural layers annular membrane by being formed at first annulus between described main body and the described laminate.
17, the film shaped method of multilayer blow moulding as claimed in claim 16, it is characterized in that described control step has: with each and temperature of setting and the step that compares by the detected temperature of being located on the described single thin film finishing die of at least one temperature sensor of the described a plurality of single thin film finishing dies of correspondence; Described a plurality of each cartridge heater of drive as a result based on the comparison are individually to be heated the step of described single thin film finishing die by the cartridge heater corresponding with described single thin film finishing die in a plurality of cartridge heaters that connect described laminate setting.
18, the film shaped method of multilayer blow moulding as claimed in claim 16, it is characterized in that, the step of described control also has the amount of gas is used in control with step from the cooling of gas supply pipe supply to cooling, described cooling connects described laminate setting with gas supply pipe, discharges the cooling gas that is used for each cooling of described a plurality of single thin film finishing dies.
19, the film shaped method of multilayer blow moulding as claimed in claim 16, it is characterized in that, each of described a plurality of single thin film finishing dies has upstream side individual layer finishing die and downstream individual layer finishing die, between described upstream side individual layer finishing die and downstream individual layer finishing die, form the ring-type path of cool air
Described control step also has by making from described cooling and flows through described ring-type path of cool air with the described cooling of gas supply pipe with gas, the step that described upstream side individual layer finishing die and described downstream individual layer are shaped and cool off.
20, as the film shaped method of each described multilayer blow moulding in the claim 16～19, it is characterized in that rack body is located at the bottom of described finishing die and is had cradle portion, this cradle portion has second annulus that is connected with described first annulus, to export described plural layers
The step of described control has: arrive the film bubble air supply pipe that the airtrapping portion between described rack body and the described laminate that is located at is provided with by connecting described laminate, to the step of described airtrapping portion delivery film bubble gas; The step of the amount of the described film bubble gas that control is supplied with to described airtrapping portion via described film bubble air supply pipe; By connecting gas nozzle that described cradle portion arrives described airtrapping portion to inner step of discharging the described film bubble gas in the described airtrapping portion from the described plural layers of described second annulus output.
21, as the film shaped method of each described multilayer blow moulding in the claim 16～19, it is characterized in that also having the step of described plural layers annular membrane being cooled off in the downstream of described finishing die.
22, the film shaped method of multilayer blow moulding as claimed in claim 21 is characterized in that, described cooling step has: in first cooling body, utilize the step of cooling air with air cooled first cooling of described plural layers annular membrane; In second cooling body in the described first cooling body downstream, utilize the ring-type cooling water flow to cool off the step of second cooling of described plural layers annular membrane; In second cooling body in the described second cooling body downstream, utilize the spraying of cooling water to cool off the step of the 3rd cooling of described plural layers annular membrane.
23, the film shaped method of multilayer blow moulding as claimed in claim 22 is characterized in that, the step of carrying out described first cooling has: the step of the described plural layers annular membrane of instrumentation; In described first cooling body, control the step of the flow of described cooling air stream based on the instrumentation temperature of described plural layers annular membrane.
24, the film shaped method of multilayer blow moulding as claimed in claim 23 is characterized in that, the step of carrying out described second cooling has the step of controlling the flow of described ring-type cooling water flow based on the instrumentation temperature of described plural layers annular membrane.
25, the film shaped method of multilayer blow moulding as claimed in claim 22, it is characterized in that, the step of carrying out described first cooling has: supply with described cooling air stream via air supply pipe to described ring-type air blow-off outlet, to be used to cooling air stream from ring-type air blow-off outlet with the air cooled step of described plural layers annular membrane; Regulate the step of the air mass flow of described cooling air stream midway at described air supply pipe; Step at the described cooling air stream of cooling off of described air supply pipe midway.
26, the film shaped method of multilayer blow moulding as claimed in claim 22 is characterized in that, the step of carrying out described second cooling has: the step of supplying with first cooling water via the first cooling water supply pipe; The step of regulating the flow of described first cooling water midway at the described first cooling water supply pipe; The step of cooling off described first cooling water midway at the described first cooling water supply pipe; Described first cooling water is stored to step in the reservoir; The step of from described first cooling water of described reservoir overflow described plural layers annular membrane being cooled off by crossing the weir.
27, the film shaped method of multilayer blow moulding as claimed in claim 22, it is characterized in that, described cooling body also has and is used for dehydrator that the moisture that is attached to from the described plural layers annular membrane of described second cooling body output is removed, and the step of carrying out described second cooling also has the step of adjusting the distance of described second cooling body and described dehydrator based on the desirable character of described plural layers annular membrane.
28, the film shaped method of multilayer blow moulding as claimed in claim 22, it is characterized in that, the step of carrying out described the 3rd cooling also has: by on every side spray second cooling water of a plurality of sprayers from described plural layers annular membrane, with the step of described plural layers annular membrane cooling; Supply with the step of described second cooling water to described a plurality of sprayers via the second cooling water supply pipe; Step at second cooling water flow of regulating described second cooling water midway of the described second cooling water supply pipe; At the described second cooling water supply pipe midway with the step of described the 3rd water quench.
Applications Claiming Priority (3)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP382947/2003 | 2003-11-12 | ||
| JP2003382947A JP2005144758A (en) | 2003-11-12 | 2003-11-12 | Method and apparatus for blow-molding multilayered film |
| JP045474/2004 | 2004-02-20 |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN1839030A CN1839030A (en) | 2006-09-27 |
| CN100455427C true CN100455427C (en) | 2009-01-28 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CNB2004800239572A Expired - Fee Related CN100455427C (en) | 2003-11-12 | 2004-11-12 | Multi-layer blown film molding machine and method of molding multi-layer blown film |
Country Status (2)
| Country | Link |
|---|---|
| JP (1) | JP2005144758A (en) |
| CN (1) | CN100455427C (en) |
Families Citing this family (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP4897290B2 (en) * | 2005-12-27 | 2012-03-14 | 四国化工株式会社 | Multilayer film forming apparatus, mold member, mold member processing method, mold assembly method |
| CN103522526B (en) * | 2013-09-30 | 2016-01-13 | 西安交通大学 | A kind of Multi-layer co-extrusion die head intelligent temperature control system and control method thereof |
| CN105415659A (en) * | 2015-11-13 | 2016-03-23 | 德阳市忠诚农膜有限公司 | Production technique for thin film |
| CN114643696B (en) * | 2022-02-22 | 2023-07-18 | 华南理工大学 | Device and method for blow molding of spiral differential runner of inner and outer mouth molds of crossed film |
Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN2177580Y (en) * | 1993-10-06 | 1994-09-21 | 何朝池 | Double mould head extruding mechanism for plastic film blowing machine |
| CN1228056A (en) * | 1997-03-31 | 1999-09-08 | 三井化学株式会社 | Multilayered laminate containing ultrahigh-molecular polyolefin layer, process for producing same, and apparatus therefor |
| JP2002079576A (en) * | 2000-09-07 | 2002-03-19 | Mitsubishi Heavy Ind Ltd | Molding equipment for blow molding multilayered film |
-
2003
- 2003-11-12 JP JP2003382947A patent/JP2005144758A/en active Pending
-
2004
- 2004-11-12 CN CNB2004800239572A patent/CN100455427C/en not_active Expired - Fee Related
Patent Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN2177580Y (en) * | 1993-10-06 | 1994-09-21 | 何朝池 | Double mould head extruding mechanism for plastic film blowing machine |
| CN1228056A (en) * | 1997-03-31 | 1999-09-08 | 三井化学株式会社 | Multilayered laminate containing ultrahigh-molecular polyolefin layer, process for producing same, and apparatus therefor |
| JP2002079576A (en) * | 2000-09-07 | 2002-03-19 | Mitsubishi Heavy Ind Ltd | Molding equipment for blow molding multilayered film |
Also Published As
| Publication number | Publication date |
|---|---|
| JP2005144758A (en) | 2005-06-09 |
| CN1839030A (en) | 2006-09-27 |
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