JP4876385B2 - Resin hollow molded container and manufacturing method thereof - Google Patents

Description

  The present invention relates to a resin hollow molded container and a method for producing the same. Specifically, it is a resin-made hollow molded container having a cap portion and a hollow body portion that is at least partially foamed, and the cap portion is substantially not foamed, so that the capping property of the plug portion is reduced. The present invention relates to a good resin hollow molded container and a method for producing the resin hollow molded container.

  Resin foam-molded products have been used in various fields for the purpose of reducing the weight of the product, improving heat insulation, and imparting functionality such as light shielding properties.

  Conventionally, as a technique for obtaining a resin foam molded article, for example, there is a method described in Patent Document 1. Specifically, this method includes (1) impregnating a thermoplastic resin with a gas such as nitrogen or carbon dioxide in a high-pressure or supercritical state in a high-pressure vessel, and then (2) heat impregnated with the gas. The plastic resin is taken out from the high-pressure vessel, heated to a temperature equal to or higher than the glass transition temperature (Tg) of the thermoplastic resin with an oil bath or the like, and (3) foaming having fine bubbles by inducing nucleation and growing bubbles. A molded product is obtained.

  Also in the resin hollow molded container, the foamed hollow molded container is similarly employed for the purpose of reducing the weight, improving the heat insulating property, and imparting the light shielding property. In many cases, the hollow molded container has a configuration in which a cap portion is provided for a hollow body portion (main body portion) serving as a housing portion and a cap is attached to the cap portion to seal the inside of the container. Is done. However, in a foamed hollow molded container, if this plug part is also a foamed part, the dimensional accuracy and shape accuracy of the plug part will be inferior due to expansion due to foaming, and it is difficult to fit the cap into the plug part. Even if the cap is fitted, the sealing performance is deteriorated.

  Therefore, in Patent Document 2, a thermoplastic molten resin containing a foaming agent is injection-molded to obtain a substantially non-foamed preform, and the portion other than the plug portion of the preform is heated to cause foaming. Then, while the heated portion is softened, a method of manufacturing a container having a substantially non-foamed cap portion by stretch blow molding has been proposed. However, the method described in Patent Document 2 requires a shielding plate for preventing only the plug portion from being heated when the preform is heated, but the plug portion is completely attached even when the shielding plate is attached. Therefore, there is a problem that some foaming occurs in the plug portion and the dimensional accuracy and shape accuracy of the plug portion are poor.

In addition, Patent Document 1 described above describes a method of obtaining a resin foam material using high pressure or supercritical gas. However, Patent Document 1 discloses a method for forming a hollow molded container in this way. In addition to the problems of dimensional accuracy and shape accuracy due to foaming of the plug portion, there is no mention of molding of a hollow molded container.
JP-T 6-506724 JP-A 61-53021

  The present invention solves the above-mentioned conventional problems, and is a lightweight resin hollow molded container to which functions such as heat insulating properties and light shielding properties are imparted by forming a hollow body portion as a foamed portion. A resin hollow molded container having excellent dimensional accuracy and shape accuracy of the plug portion and having good sealing performance by capping, and a method for producing this resin hollow molded container The purpose is to provide.

The method for producing a resin hollow molded container according to the present invention (Claim 1 ) includes a step of molding a preform of a resin hollow molded container having a cap portion using a raw material resin containing polyethylene terephthalate , and the preform. Contacting the pressurized gas in a supercritical state at a temperature below the softening point of the raw material resin to dissolve the gas in the preform, and the preform in which the gas is dissolved at a temperature below the glass transition point of the raw material resin A process for producing a resin hollow molded container comprising a step of returning to normal pressure and a step of heating and stretching the preform, wherein the raw material resin does not substantially contain a foaming agent, and is applied to the preform. prior to the step of dissolving the gas, have a step of heating crystallized mouth portion of the preform, the density of the mouth portion after crystallization and wherein 1.35 g / cm ³ or more der Rukoto That.

The method for producing a resin hollow molded container according to claim 2 is characterized in that, in claim 1 , the pressurized gas is carbon dioxide gas.

The resin hollow molded container of the present invention (Claim 3 ) is also characterized by being manufactured by the above-described method for manufacturing a resin hollow molded container of the present invention.

  According to the present invention, it is a lightweight resin hollow molded container to which functions such as heat insulation and light shielding properties are imparted by making the hollow body part a foamed part, and the plug part is a non-foamed part or By being a low foaming part, the resin hollow molding container which is excellent in the dimensional accuracy and shape precision of the stopper part, and has favorable sealing performance by capping is provided.

  Hereinafter, embodiments of the resin hollow molded container and the manufacturing method thereof according to the present invention will be described in detail according to the method of manufacturing the resin hollow molded container according to the present invention. It is a typical example of this embodiment, and the present invention is not limited to these contents.

[Method for producing resin hollow molded container]
[1] Resin species constituting the resin hollow molded container of starting resin this invention is a thermoplastic resin, as its thermoplastic resin, Fang aromatic polyesters, aliphatic polyesters, polyester-based, such as the cycloaliphatic polyester etc. tree butter, and the like. These may be used alone or in combination of two or more.

  Among them, the crystalline resin is preferable because the effect of improving the strength is exhibited by the stretching effect when the hollow resin molded container is stretch blow molded, the polyester resin is more preferable, and the polyethylene terephthalate is particularly preferable.

  Therefore, in the method for producing a resin hollow molded container of the present invention, it is preferable to use a polyester-based resin as the raw material resin, and more preferably to use polyethylene terephthalate.

  In the raw material resin according to the present invention, various resin additives can be blended as necessary within a range not impairing the effects of the present invention. Examples of resin additives include foam nucleating agents, colorants such as pigments and dyes, heat stabilizers, light stabilizers, mold release agents, preservatives, ultraviolet absorbers, plasticizers, lubricants, flame retardants, and conductivity imparting. Agents, antistatic agents, crystal nucleating agents and the like. These resin additives may be used alone or in combination of two or more.

  However, in the method for producing a resin hollow molded container according to the present invention, a raw material resin that does not substantially contain a foaming agent is used.

  Here, the foaming agent is a general term for chemicals used to form a group of bubbles fixed in a resin molded body, for example, a gas or a volatile liquid, an inorganic that decomposes by heating to generate a gas. Or an organic compound etc. are used. More specifically, physical foams such as inert gases such as nitrogen, carbon dioxide and helium, saturated hydrocarbons such as propane, butane, pentane and hexane, halogenated hydrocarbons such as tetrafluoroethane and freon (trade name) Chemicals such as chemicals, inorganic salts such as sodium carbonate and sodium bicarbonate, organic salts such as sodium citrate, azo compounds such as azodicarbonamide and hydrazonecarbonamide and their salts, tetrazole compounds such as 5-phenyltetrazole and their salts A foaming agent is mentioned.

  In the present invention, the raw material resin substantially not containing a foaming agent is a raw material resin not actively mixed with a foaming agent in preparation of the raw material resin, and is inevitably mixed in the preparation step of the raw material resin. A very small amount of gas, residual solvent, or the like does not correspond to the foaming agent in the raw material resin according to the present invention. Further, examples of the above-mentioned foam nucleating agent include glass, mineral materials, etc., and these serve as nuclei to promote the start of foaming, and the foam nucleating agent itself does not foam. It is different from the agent.

[2] Molding of preform In the method for producing a resin hollow molded container according to the present invention, first, a preform (precursor) of a resin hollow molded container having a plug portion is molded using the raw material resin. The preform molding method includes, for example, a method of molding a test tubular preform with a plug portion by injection molding of a raw material resin, an extrusion molding of the raw material resin into a tube shape, and cutting this into a plug portion and a bottom portion. And the like may be formed by hot press molding. Note that the plug portion usually has a support ring for supporting the pressure received from above during capping or for use during transportation. This support ring can be provided by providing a gap corresponding to the support ring in an injection mold or press mold used when molding a preform.

[3] Heating and Crystallization of Mouth Portion Next, the plug portion of the preform obtained is heated and crystallized. That is, only the plug portion of the preform is heated to a temperature equal to or higher than the crystallization temperature of the raw material resin for crystallization.

  This heating temperature is preferably 0 to 20 ° C. higher than the crystallization temperature of the resin, for example, 170 to 190 ° C. if the raw material resin contains polyethylene terephthalate. If the crystallization temperature is too low, sufficient crystallization cannot be achieved, and if it is too high, the resin is deteriorated. The heating time may be a time during which the plug portion is crystallized, but is usually about 2 to 5 minutes.

  In addition, as a method of heating only the plug portion of the preform, specifically, a portion of the aluminum pot that is below the support ring of the preform is shielded so that heat is not applied, and infrared rays are applied. What is necessary is just to heat only a plug part using a heater.

By crystallization of the plug part in this manner, when polyethylene terephthalate is used as the raw material resin, the density of the plug part after crystallization is 1.35 g / cm ³ or more, particularly 1. It is preferably 36 g / cm ³ or more, particularly 1.37 g / cm ³ or more. When the density of the plug portion after crystallization is less than 1.35 g / cm ³ , the gas is dissolved not only in the trunk portion of the preform but also in the plug portion in the step of dissolving the gas in the preform of the subsequent step. Since it becomes easy to melt | dissolve, foaming of a plug part occurs in a subsequent process and the objective of this invention cannot be achieved. In addition, the upper limit of the density of the plug portion after crystallization is usually 1.42 g / cm ³ .

[4] Dissolution of gas in preform The preform crystallized from the plug portion is then brought into contact with a pressurized gas at a temperature equal to or lower than the softening point of the raw material resin to dissolve the gas in the preform. Specifically, the preform is placed in a pressure vessel, gas is pressurized and injected into the pressure vessel, and the preform is brought into contact with the pressurized gas to dissolve the gas in the preform. In this gas dissolving step, the gas is dissolved only in the body portion of the preform, and the gas is not substantially dissolved in the crystallized plug portion.

(1) Temperature conditions The temperature at which the gas is dissolved in the preform is set in a temperature range from normal temperature (that is, 10 to 25 ° C.) to the softening point of the raw resin. Preferably it is above normal temperature and below the glass transition point of the raw material resin. If this temperature is lower than normal temperature, the gas is difficult to dissolve in the preform, and if the temperature is too high, the shape of the preform is destroyed, which is not preferable.

  In the present invention, the softening point means a melting peak temperature (Tm) measured by a differential scanning calorimeter (DSC) in accordance with JISK7121, and the glass transition point is measured in accordance with JISK7121. Glass transition temperature (Tg). In the case of polyethylene terephthalate, Tm is generally about 258 ° C. and Tg is about 80 ° C.

  Therefore, when polyethylene terephthalate is used as the raw material resin, the temperature condition of this gas dissolving step is preferably about 10 to 80 ° C.

(2) Pressure condition The reason for pressurizing the gas in the gas dissolving step is to increase the amount of gas dissolved in the preform. The higher the gas pressure, the larger the amount dissolved in the preform, but this is not preferable because the apparatus becomes large. Therefore, the pressure condition is preferably set in a range exceeding normal pressure and 40 MPa or less, for example, in a range of 5 to 35 MPa.

(3) Contact time The contact time between the preform and the gas is the type of raw material resin used, the size of the preform, the thickness of the preform (the thickness of the wall constituting the hollow body of the preform), The type of gas used, the pressure when contacting the gas, the temperature when contacting the gas, the form of the foamed part of the hollow resin molded container to be finally obtained (foaming ratio, bubble density, bubble size) ) And the like can be appropriately set within a range of several seconds to several hours.

(4) Gas type The gas used is preferably a gas inert to the raw material resin. Here, the gas inert to the raw material resin refers to a gas that does not lower the physical properties of the raw material resin or change the chemical structure by bringing the gas into contact with the raw material resin.

  Specific examples of the gas include argon, nitrogen, carbon dioxide, and the like. Among these, carbon dioxide is preferable from the viewpoint that it can be easily handled in a supercritical state described later.

(5) Gas State Although the gas may be in a pressurized gas state, a subcritical state or a supercritical state is preferable, and it is particularly preferable to contact the preform in the supercritical state. The supercritical state means a state above the critical temperature and critical pressure. For example, in the case of carbon dioxide, the supercritical state is a state where the temperature is 30 ° C. or higher and the pressure is 7.3 MPa or higher. The gas in the supercritical state has a property that it has a lower viscosity than that in the liquid state and easily diffuses into the resin, and has a higher density than the gas state. This is preferable because it can be dissolved in the reform.

  Therefore, when carbon dioxide is dissolved in a preform using polyethylene terephthalate as a raw material resin, it is preferable that carbon dioxide is brought into contact with the preform under conditions of about 7.3 to 40 MPa at 10 to 30 ° C.

(6) Amount of dissolved gas The larger the amount of dissolved gas in the preform, the higher the expansion ratio and the more bubbles can be formed. The amount of the gas dissolved in the preform increases as the surface layer portion of the wall (that is, the portion in the vicinity of the wall surface) constituting the body portion of the preform increases, and decreases as it moves toward the inner layer portion (inside the wall). Therefore, the amount of dissolved gas in the preform can be inclined in the thickness direction of the wall, but it is preferable to adjust the gas so that it does not reach the center in the thickness direction of the wall of the preform. This is because a non-foamed layer is formed at the center of the wall in a later step to ensure the strength of the resulting resin hollow molded container.

  As an example of a method for preventing the gas from reaching the center layer of the preform wall, when the dissolution distance of the gas is x, the diffusion coefficient of the gas within the preform wall is D, and the dissolution time is t, Since x = √ (Dt), a method of setting t so that x is smaller than the center portion in the thickness direction from the surface of the preform wall (that is, 1/2 of the wall thickness). However, it is also possible to obtain a suitable time in advance by experiments.

  In addition, since the amount of dissolved gases affects the form of the foamed layer (foaming ratio, bubble density, bubble size) of the resulting resin hollow molded container, the resin hollow molded container is manufactured industrially. In this case, it is preferable to set the manufacturing conditions by confirming the optimum conditions in the process of dissolving the gas in the preform by experiments.

[5] Depressurization of preform After the preform is brought into contact with the pressurized gas to dissolve the gas, the preform is depressurized at a temperature not higher than the glass transition point of the raw material resin and returned to normal pressure. In this step, if the temperature of the preform is higher than the glass transition point of the raw material resin, foaming may occur in the step-down step, which is not preferable. When polyethylene terephthalate is used as the raw material resin, the temperature condition of the pressure-lowering step is preferably 10 to 70 ° C.

  Although there is no particular limitation on the step-down speed, it takes a long time to return to normal pressure when the step-down speed is slow. On the other hand, when trying to increase the pressure reduction speed, it is preferable to set the pressure reduction speed at about 5 to 20 MPa / min because the decompression pipe needs to be thickened.

[6] Heat stretching of preform After the pressure reduction, the preform in which the gas is dissolved is heat stretched, that is, stretch blow molded to obtain a resin hollow molded container.

  The heating temperature at this time is not less than the glass transition point of the raw material resin. If this temperature is less than the glass transition point of the raw material resin, stretch molding cannot be performed, but if it is too high, the resin will deteriorate. When polyethylene terephthalate is used as the raw material resin, the stretch blow molding temperature is preferably 90 to 110 ° C.

  In this heat stretching, foaming occurs in the body portion of the preform in which the gas is dissolved, and a foam layer is formed. On the other hand, foaming does not occur in the plug portion where the gas is not substantially dissolved.

  Further, as described above, the amount of gas dissolved in the preform is inclined in the thickness direction of the preform wall, and is large on the surface layer side and small on the inner layer side. In particular, in the present invention, the gas is preferably dissolved so as to form a portion where the gas is not dissolved in the central portion of the body portion in the thickness direction. Therefore, it is preferable that the resin hollow molded container obtained by this heat-stretching has a layered structure in which the central portion in the thickness direction is a non-foamed layer and the foamed layers are formed on the surface layers on both sides of the body portion. Here, as described above, the thickness of the central non-foamed layer can be easily controlled by adjusting the amount of gas dissolved in the preform, that is, the dissolution conditions.

  In addition, the outermost surface layer in the thickness direction of the body portion may break after foaming to become a non-foamed layer. Further, the foam size of the foam layer formed on the body portion tends to be larger on the center side and smaller on the surface layer side in the thickness direction. Therefore, the resin hollow molded container obtained by the present invention is usually one of the outermost layer non-foamed layer / foamed layer / central layer non-foamed layer / foamed layer / the other in the thickness direction in the body portion. The outermost non-foamed layer has a sandwich structure in this order, and the bubble diameter of the foamed layer gradually increases from the center layer side to the surface layer side.

  In the present invention, the non-foamed layer refers to a layer in which only bubbles having an average bubble diameter of less than 0.1 μm are observed when the cross section of the hollow molded container is observed with a scanning electron microscope magnified 60 times. The layer refers to a layer in which bubbles having an average bubble diameter of 0.1 μm or more are observed when the cross section of the hollow molded container is observed with a scanning electron microscope magnified 60 times.

[Hollow resin molded container]
Next, the resin hollow molded container of the present invention will be described.

  The resin hollow molded container according to the present invention is a resin hollow molded container having a cap portion and a hollow barrel portion, wherein at least a part of the barrel portion is a foamed portion, and the foaming ratio of the plug portion is a barrel. It is characterized by being lower than the expansion ratio of the foamed part of the part, or the plug part being substantially not foamed.

  The resin hollow molded container is preferably manufactured by the above-described method for manufacturing a resin hollow molded container according to the present invention, but is not limited to the method for manufacturing a resin hollow molded container according to the present invention. Resin is used as a raw material to form a preform of a resin hollow molding container having a cap portion by injection molding or extrusion molding, and the gas is impregnated and dissolved by contacting a pressurized gas only to the body of the preform. It can also be obtained by heating and foaming and stretching and blowing to form a hollow molded container.

  The plug portion of the resin hollow molded container of the present invention has a foaming ratio lower than the foaming ratio of the foamed portion of the trunk or is not substantially foamed. When the expansion ratio of the plug portion is equal to or higher than the expansion ratio of the foamed portion of the body portion, the dimensional accuracy and shape accuracy of the plug portion are inferior, so that the fitting of the cap is deteriorated and the tightness of the container is deteriorated. It is preferable that the plug portion is not substantially foamed.

  Here, the expansion ratio is the density (D1) of an arbitrary part in the preform of the hollow molded container and the density (D2) of the part corresponding to the arbitrary part of the preform of the molded hollow resin container after molding. Is a value obtained by dividing the obtained density D1 by the density D2. “Not substantially foamed” means that the value of D1 / D2 is, for example, about 1 to 1.05.

Moreover, the resin hollow molded container of the present invention is preferably made of a polyester-based resin, particularly polyethylene terephthalate. When the resin is polyethylene terephthalate, the density of the plug portion is 1.35 g / cm ³ or more. Is preferred. If the density of the plug portion is less than 1.35 g / cm ³ , the degree of crystallinity of polyethylene terephthalate tends to be low and the dimensional stability tends to be inferior to heat, and the dimensional accuracy and shape accuracy of the resulting resin hollow molded container May be inferior.

  Further, the foamed portion of the body portion of the resin hollow molded container of the present invention has a layered structure of a foamed layer and a non-foamed layer in the thickness direction of the wall, the surface layer side is a foamed layer and the central portion in the thickness direction is A non-foamed layer is preferred. That is, the foamed layer contributes to the weight reduction of the container, the improvement of the functionality such as heat insulation, and the like, while the non-foamed layer contributes to the strength and heat resistance retention of the container. When the wall constituting the body of the resin hollow molded container has a layered structure in which the central portion in the thickness direction is a non-foamed layer and the surface layer portions on both sides are formed of a foamed layer, sufficient strength and heat resistance can be obtained. It is preferable because a resin-made hollow molded container having a light weight and excellent functionality such as heat insulation can be obtained.

  In this case, the thicknesses of the foamed layer and the non-foamed layer forming this layered structure can be arbitrarily set according to the required characteristics of the resin hollow molded container.

  For example, the strength and heat resistance can be increased by increasing the thickness of the non-foamed layer of the center layer. Further, by reducing the thickness of the non-foamed layer of the center layer and the foamed layer of the surface layer, the weight can be reduced and the heat insulation can be improved. In order to obtain a resin-made hollow molded container with improved heat insulation, it is preferable to use 30% or more of the total thickness of the wall portion of the body portion as the foam layer. In order to improve heat resistance, when the resin is a crystalline resin such as polyethylene terephthalate, it is preferable that the crystallinity is high, and the crystallinity is 5% or more, and more preferably 10% or more. Moreover, in order to improve heat resistance, it is preferable that the thickness of the non-foamed layer of the center layer is in the range of 10 to 90%, particularly in the range of 20 to 50% of the total thickness of the wall portion of the trunk portion.

  Hereinafter, the present invention will be described more specifically with reference to examples and comparative examples. However, the present invention is not limited to the following examples as long as the gist thereof is not exceeded.

  In the following, measurement of the surface temperature of the preform and the surface temperature of the plug portion is performed using a non-contact handy thermometer “IT2-80” manufactured by Keyence Corporation with an emissivity of 0.90. The surface temperature after the heat treatment was measured from a distance of about 0.3 m.

Example 1
A resin hollow molding container was molded in the following direction using polyethylene terephthalate (“RT553” manufactured by Nihon Unipet Co., Ltd., glass transition point (Tg) 80 ° C.) as a raw material resin.

  First, about 5 kilograms of raw material polyethylene terephthalate is placed flat in a stainless steel bat measuring approximately 300 × 500 × 80 mm in length × width × height, and about 12 hours at 145 ° C. using a vacuum dryer “DP63” manufactured by Yamato Scientific Co., Ltd. Was vacuum dried. For the purpose of preventing moisture absorption during molding, the raw material resin after the vacuum drying was put into a resin dryer “Challenger D-50” manufactured by Kawata Co., Ltd., and a preform was injection molded while being held at 135 ° C.

  Injection molding uses a multilayer stretch blow machine injection molding machine (manufactured by Nissei ASB Co., model: ASB-50TH), the cylinder set temperature and the hot runner set temperature are 280 ° C., and the injection is 1.5 seconds. A preform having a length of 100 mm, an outer diameter of 25 mm, and a body wall thickness of 4 mm, having a stopper part with a support ring under the conditions of pressure holding of 16.5 seconds, cooling of 10 seconds and mold temperature of 15 ° C. (internal capacity of 30 ml) )created. When this preform was visually confirmed, no bubbles were observed.

The plug crystallizer (Nissei A.S. Co., Ltd.) was constructed so that only the plug part was heated by inserting the part below the support ring of the obtained preform into an aluminum cylindrical pot. -“M-2000” manufactured by B Machine Co., Ltd.), adjusting the heater output so that the temperature immediately after the heating of the surface of the plug portion of the preform charged at room temperature is 183 ± 2 ° C., and the production rate is 1800 The mouthpiece was crystallized as a book / hour. The density of the crystallization plug obtained at this time was measured at 23 ° C. using a sample obtained by cutting the plug into a square of about 5 mm and a density gradient tube made of sodium bromide in water / ethanol. As a result, the density of the top surface of the plug portion was 1.385 g / cm ³ , and the density of the support ring portion of the plug portion was 1.360 g / cm ³ .

  Next, the preform obtained by crystallizing the obtained plug part is accommodated in a pressure-resistant container having a capacity of 1000 ml, the atmospheric temperature is set to 30 ° C., and carbon dioxide pressurized to 25 MPa is injected into the pressure-resistant container. The preform and pressurized carbon dioxide were brought into contact with each other while being kept under pressure for 2 hours. Thereafter, pressurized carbon dioxide was returned to normal pressure at 25 ° C. over 5 minutes to obtain a preform in which carbon dioxide was dissolved.

  Next, molding was performed using this preform. In the molding machine, the preform moves 90 degrees each in the order of the preform charging unit and bottle take-out unit, the primary heating unit equipped with a near infrared heater, the secondary heating unit, and the blow molding unit to form a stretch blow bottle. A rotary stretch blow molding machine (manufactured by Hubei Seiko Co., Ltd.) was used. The primary heating time of the preform was set to 46 seconds, the secondary heating time was set to 23 seconds, and the cooling time after the completion of the secondary heating in the secondary heating unit was set to 23 seconds. Thereby, the preform surface temperature of a primary heating part and a secondary heating part will be 90-100 degreeC, 110-120 degreeC, respectively, and preform surface temperature will be 100 degreeC-110 degreeC by standing_to_cool. Here, pressurized air of 3 MPa is injected, the length is about 200 mm, the outer diameter is about 60 mm, the average thickness is about 1 mm, the inner volume is 500 ml, and the inner and outer surface layers of the barrel and the thickness central portion of the barrel are A polyester resin hollow molded container having a multi-layer structure, which was a non-foamed layer and the portion sandwiched between the surface layer and the central portion was composed of a foamed layer, was obtained.

  In the mouthpiece part of the obtained polyester resin hollow molded container, foaming was not seen in the top surface part and the support ring part (foaming ratio 1), and the appearance was very good. Moreover, 70% of the trunk portion in the thickness direction is a non-foamed layer, and the remaining portion is a foamed layer, and the foaming ratio was 1.1 times as "total of foamed layer and non-foamed layer". The foaming ratio was calculated to be 1.4 times.

  When the obtained container was capped with a cap BBW-E8-612 made by Shibazaki Seisakusho Capping Machine 501 with Magna Torque Head VK560 and made by Shibazaki Seisakusho Co., Ltd. Sealability was obtained.

(Comparative Example 1)
In Example 1, a polyester resin hollow molded container was obtained in the same manner as in Example 1 except that the plug crystallization step was omitted, and capping was attempted in the same manner.

In Comparative Example 1, the density of the plug portion of the preform subjected to the gas dissolving step was 1.336 g / cm ³ , and the plug portion of the obtained resin hollow molded container had foaming (foaming) The magnification was 1.1 times), and the cap could not be properly fitted.

  The resin hollow molded container provided by the present invention is lightweight and excellent in heat insulation and light shielding properties, and can be used for a wide variety of applications such as beverage containers, food containers, cosmetic containers, detergents, and other pharmaceutical containers. .

Claims (3)

Forming a preform of a resin hollow molding container having a cap portion using a raw material resin containing polyethylene terephthalate ;
Contacting the preform with a pressurized gas in a supercritical state at a temperature below the softening point of the raw resin to dissolve the gas in the preform;
Returning the preform in which the gas is dissolved to a normal pressure at a temperature below the glass transition point of the raw resin,
Thereafter, a method for producing a resin hollow molding container having a step of heating and stretching the preform,
The raw material resin is substantially free of blowing agent and prior to the step of dissolving a gas into said preform, have a step of heating crystallized mouth portion of the preform, the mouth after crystallization method for producing a resin hollow molded containers density of the plug portion, characterized in der Rukoto 1.35 g / cm ³ or more. The method for producing a resin hollow molded container according to claim 1 , wherein the pressurized gas is carbon dioxide. A resin hollow molded container produced by the method according to claim 1 .