Cup-type container and method of forming the same
09717355 · 2017-08-01
Assignee
Inventors
- Toshifusa Azuma (Kanagawa, JP)
- Yutaka Asano (Kanagawa, JP)
- Shigenori Ueda (Kanagawa, JP)
- Motohiko Shimada (Tokyo, JP)
- Masaru Yamaguchi (Tokyo, JP)
Cpc classification
B29C2043/5825
PERFORMING OPERATIONS; TRANSPORTING
B29C43/58
PERFORMING OPERATIONS; TRANSPORTING
B29C2043/5833
PERFORMING OPERATIONS; TRANSPORTING
B29C43/34
PERFORMING OPERATIONS; TRANSPORTING
B65D1/26
PERFORMING OPERATIONS; TRANSPORTING
B29C43/02
PERFORMING OPERATIONS; TRANSPORTING
International classification
A47G19/22
HUMAN NECESSITIES
B29C43/34
PERFORMING OPERATIONS; TRANSPORTING
B29C43/58
PERFORMING OPERATIONS; TRANSPORTING
B29C43/20
PERFORMING OPERATIONS; TRANSPORTING
B29C43/02
PERFORMING OPERATIONS; TRANSPORTING
Abstract
A cup-type container obtained by compression-forming a thermoplastic resin and including at least a flange portion, a body portion and a bottom portion, wherein a ratio (L/D) of the height of the container to the diameter of the opening is not less than 1.0, and if the direction of height of a test piece cut out from the body portion of the container is denoted by x and the circumferential direction thereof by y, a half-value width P at a half peak of a Miller index at a diffraction angle 2θ=14.5° that represents the diffraction by the crystal plane (110), is in a range of 1.25 to 1.5 over the whole body portion in a peak intensity profile in the direction of height (x-direction) of a Debye's ring obtained by measuring the diffraction intensities by causing the X-rays to be incident on an x-y plane of the test piece at right angles thereto. The cup-type container is evenly oriented in the direction of height of the container and in the circumferential direction thereof, has an even strength in all directions and has excellent heat resistance. The invention, further, provides a method of forming the cup-type container.
Claims
1. A compression-formed thermoplastic resin container comprising: at least a flange portion; an opening having a diameter (D); a body portion; a bottom portion; and a container height (L), wherein a ratio (L/D) of the container height (L) to the diameter (D) of the opening is not less than 1.0, and wherein, when a direction of height of a test piece cut out from the body portion of the container is denoted by “x” and a circumferential direction thereof by “y”, a half-value width (P) at a half peak of a Miller index at a diffraction angle 2θ=14.5° that represents a diffraction by a crystal plane (110), is in a range of 1.25 to 1.5 over a whole of the body portion in a peak intensity profile in a direction of height (x-direction) of a Debye's ring obtained by measuring diffraction intensities by causing X-rays to be incident on an x-y plane of the test piece at right angles thereto.
2. A compression-formed thermoplastic resin container comprising: at least a flange portion; a body portion; and a bottom portion, wherein a rate of change (K) of half-peak widths is represented by formula K=P.sub.2/P.sub.1, with K being in the range of 0.95 to 1.05, with P.sub.1 being a half-peak width at a measuring point at a center of the bottom portion and with P.sub.2 being a half-peak width at a measuring point on the bottom portion, wherein, when a radius of the bottom portion is denoted by “R” and a distance from the measuring point at a center of the bottom portion is denoted by “r”, a radius ratio (r/R) is >0.7, and wherein, when a radial direction of a test piece of the bottom portion cut out from the measuring point is denoted by “x” and a circumferential direction thereof by “y”, then half-values are widths at a half peak of a Miller index at a diffraction angle 2θ=14.5° that represents diffraction by a crystal surface (110) in a peak intensity profile in a radial direction (x-direction) of a Debye's ring obtained by measuring diffraction intensities by causing X-rays to be incident on an x-y plane of the test piece at right angles thereto.
3. The container of claim 1, wherein all of the body portion and the bottom portion comprise a multi-layer structure.
4. The container of claim 2, wherein all of the body portion and the bottom portion comprise a multi-layer structure.
5. The container of claim 3, wherein the multi-layer structure comprises at least inner and outer layers of a polypropylene and an intermediate layer of another thermoplastic resin, the inner and outer layers completely covering the intermediate layer so that the intermediate layer is not exposed to a surface of the container.
6. The container of claim 4, wherein the multi-layer structure comprises at least inner and outer layers of a polypropylene and an intermediate layer of another thermoplastic resin, the inner and outer layers completely covering the intermediate layer so that the intermediate layer is not exposed to a surface of the container.
7. The container of claim 1, wherein the body portion comprises an inner layer, an intermediate layer and an outer layer, and has a ratio of thickness range of inner surface side:outer surface side equal to between 3:7 and 6:4, with the inner side being a thickness from an inner surface to a center of a thickness of the intermediate layer and with the outer side being a thickness from an outer surface to the center of thickness of the intermediate layer.
8. The container of claim 2, wherein the body portion comprises an inner layer, an intermediate layer and an outer layer, and has a ratio of thickness range of inner surface side:outer surface side equal to between 3:7 and 6:4, with the inner side being a thickness from an inner surface to a center of a thickness of the intermediate layer and with the outer side being a thickness from an outer surface to the center of thickness of the intermediate layer.
9. The container of claim 1, wherein the body portion comprises a stacking step formed in one of: an inner surface of the body portion; and an outer surface of the body portion.
10. The container of claim 2, wherein the body portion comprises a stacking step forming in one of: an inner surface of the body portion; and an outer surface of the body portion.
11. The container of claim 1, wherein a thickness of the body portion is not more than 2.0 mm.
12. The container of claim 2, wherein a thickness of the body portion is not more than 2.0 mm.
Description
BRIEF DESCRIPTION OF THE DRAWINGS
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CUP-TYPE CONTAINERS
(16) The cup-type container of the present invention includes at least a body portion and a bottom portion, the body portion including a portion where the thickness is not less than 1.0 mm, and, preferably, has a ratio (L/D) of the height (L) of the container and the diameter (D) of the opening of not less than 1.0 and, specifically, in a range of 1.5 to 2.0.
(17) In the invention, the body portion may have a thickness of not less than 1.0 mm in only a portion thereof in the direction of height or may have a thickness of not less than 1.0 mm over the whole body portion. Specifically, as will be concretely described later, it is desired that the body portion has a thickness (t1 in
(18) The cup-type container can employ various structures, and though not limited thereto only,
(19) Further, in the cup-type container of the multi-layer structure having inner and outer layers of a thermoplastic resin and an intermediate layer of a gas-barrier resin as represented by a portion X on an enlarged scale in an inset in
(20) Further, in the body portion as represented by a portion Y on an enlarged scale in an inset of
(21) (Thermoplastic Resins)
(22) The cup-type container of the invention may comprise a single layer of a thermoplastic resin. Desirably, however, the cup-type container has a multi-layer structure inclusive of an intermediate layer formed by using a functional resin such as gas-barrier resin, oxygen-absorbing resin or water vapor-barrier resin.
(23) In the case of the single layer or the multi-layer structure, the inner and outer layers can be constituted by using a thermoplastic resin such as polyolefin resin, polyester resin, polystyrene resin, polyamide resin or polycarbonate resin though not limited thereto only.
(24) As the polyolefin resin, there can be exemplified low-, intermediate- and high-density polyethylenes, homopolypropylene, random polypropylene, blocked polypropylene, isotactic polypropylene, syndiotactic polypropylene, propylene-ethylene copolymer, ethylene-vinyl acetate copolymer, ethylenically unsaturated carboxylic acid, and olefin resins graft-modified with the anhydrides thereof.
(25) As the polyester resin, there can be particularly preferably used a polyester that is chiefly constituted by using a polyethylene terephthalate. Namely, there can be preferably used a polyester that contains the ethylene terephthalate unit in an amount of not less than 80 mol % and, specifically, not less than 90 mol %, and other copolymerizable components such as isophthalic acid, 2,6-naphthalenedicarboxylic acid, 1,4-butanediol and 1,4-cyclohexanedimethanol.
(26) As the polycarbonate resin, there can be exemplified a carbonic acid ester resin derived from bicyclic divalent phenols or phosgenes, i.e., a polycarbonate derived from bisphenols such as 2,2′-bis(4-hydroxyphenyl) propane (bisphenol A), 2,2′-bis(4-hydroxyphenyl) butane (bisphenol B), or 1,2-bis(4-hydroxyphenyl) ethane.
(27) The present invention uses, preferably, a polypropylene and, specifically, a random polypropylene from the standpoint of compression formability. It is desired that the polypropylene has a melt flow rate (MFR) in a range of 5 g/10 min. to 30 g/10 min. and, specifically, 10 g/10 min. to 20 g/10 min.
(28) The thermoplastic resin used in the invention can be blended with blending agents known per se., such as antioxidant, heat stabilizer, ultraviolet ray absorber, antistatic agent, filler, lubricant and inorganic or organic coloring agent.
(29) (Resins for Forming the Intermediate Layer)
(30) [Gas-Barrier Resins]
(31) A representative example of the gas-barrier resin is an ethylene-vinyl alcohol copolymer like, preferably, a saponified product of a copolymer obtained by saponifying an ethylene-vinyl acetate copolymer that contains an ethylene in an amount of 20 to 60% by mole and, specifically, 25 to 50% by mole such that the saponification degree is not less than 96% and, specifically, not less than 99 mol %.
(32) As the gas-barrier resins other than the ethylene-vinyl alcohol copolymer, there can be exemplified amides such as nylon 6, nylon 6.6, nylon 6/6.6 copolymer, metaxylylene diadipamide (MXD6), nylon 6.10, nylon 11, nylon 12 and nylon 13. Among these polyamides, preferred ones have amide groups in a number in a range of 5 to 50 and, specifically, 6 to 20 per 100 carbon atoms.
(33) [Oxygen-Absorbing Resins]
(34) As the oxygen-absorbing resin, there can be exemplified a resin composition comprising at least an oxidizing organic component and a transition metal catalyst (oxidizing catalyst).
(35) The resin composition that includes the oxidizing organic component and the transition metal catalyst may comprise the oxidizing organic component and the transition metal catalyst only but may, further, contain resins other than the above resin, as a matter of course.
(36) As the resins that can be used in combination with the oxidizing organic component and the transition metal catalyst, there can be exemplified the above-mentioned polyolefin resins and gas-barrier resins, and, specifically, the ethylene-vinyl alcohol copolymers and the polyamides (particularly, a xylylene group-containing polyamide resin having a terminal amino group concentration of not less than 40 eq/10.sup.6 g).
(37) As the oxidizing organic component, there can be used those that have heretofore been used for the oxygen-absorbing resins; i.e., there can be exemplified ethylenically unsaturated group-containing polymers though not limited thereto only.
(38) As the transition metal type catalyst, there can be preferably used metals of the Group VIII of the periodic table, such as iron, cobalt, nickel and the like. However, there can be further used metals of the Group I such as copper, silver or the like, metals of the Group IV such as tin, titanium, zirconium or the like, metals of the Group V such as vanadium or the like, metals of the Group VI such as chromium or the like, or metals of the Group VII such as manganese or the like.
(39) It is desired that the transition metal type catalyst is contained in the oxygen-absorbing resin in such an amount that the concentration of the transition metal atoms (weight concentration basis) is in a range of 100 to 3000 ppm.
(40) [Other Functional Resins]
(41) As the functional resin that can be used as the intermediate layer of the cup-type container of the invention, there can be exemplified cyclic olefin resins and liquid crystal polymers in addition to the above-mentioned gas-barrier resins and the oxygen-absorbing resins.
(42) The cyclic olefin resins, usually, have properties such as heat resistance, moisture resistance and water vapor-barrier property that are superior to those of the general-purpose thermoplastic resins. By using the cyclic olefin resin, it is allowed to impart excellent properties to the multi-layer structure.
(43) Further, the liquid crystal polymers, usually, have properties such as rigidity, heat resistance and barrier property that are superior to those of the general-purpose thermoplastic resins. By using the liquid crystal polymer, therefore, it is allowed to impart excellent properties to the multi-layer structure.
(44) [Adhesive Resins]
(45) In the cup-type container having the multi-layer structure of the invention, adhesive layers can be formed, as required, among the intermediate layer and the inner and outer layers. As the adhesive resin, there can be used acid-modified polyolefins such as acid-modified polypropylene, acid-modified high-density polyethylene, acid-modified low-density polyethylene and acid-modified ethylene-vinyl acetate copolymer to which only, however, the invention is in no way limited.
(46) (Forming Method)
(47) In the method of forming the cup-type container of the present invention, a melt of a thermoplastic resin alone, such as polypropylene or a melt of a thermoplastic resin and other thermoplastic resin such as gas-barrier resin, is continuously extruded from an extruder and is cut by a cutting means of a known synthetic resin feeding machine to thereby prepare a molten resin mass which is in a molten state. The molten resin mass is held by a holding means, is thrown into the lower metal mold of a compression-forming machine via a guide means, is compression-formed by the upper metal mold and the lower metal mold, and is cooled and solidified to form a cup-type container. Here, in the present invention, in particular, an important feature resides in that the rate of compression is not more than 100 mm/sec and, specifically, lies in a range of 20 to 50 mm/sec at a point 5 mm before the point where the formation is completed (arrow Z in
(48) By changing the rate of shearing the resin and controlling the flow of the resin in the direction of height as described above, therefore, it is allowed to suppress the resin from being oriented in the direction of height and, therefore, to impart nearly isotropic orientation creating a parabolic flow of the resin so that the intermediate layer can be reliably extended up to the flange portion.
(49) In the invention, the rate of compression contributes most to the formability at a point just before the movement of the upper metal mold or the lower metal mold is completely finished. Therefore, the moving velocity of the metal mold is referred to at a point 5 mm before the point where the forming is completed. There is no particular limitation concerning the lower limit of the rate of compression forming. From the standpoint of productivity on an industrial scale, however, the lower limit in the rate of the compression forming should be within the above-mentioned range.
(50) In the invention as shown in
(51)
(52) In the invention, it is particularly desired that the molten resin mass fed into the lower metal mold has such a size that it comes in contact with almost all the surface of the portion defining the bottom portion of the lower metal mold.
(53) This suppresses the occurrence of uneven molecular orientation caused as the molten resin mass is partly cooled, and makes it possible to impart nearly isotropic orientation.
(54)
(55) Referring to
(56) Referring to
(57) In the invention, it is desired that the diameter of the molten resin mass is based on the strand diameter (D2) of the preset molten resin, and is compared with the diameter (D1) at a position corresponding to the outermost end of the grounding portion of the cup-type container in the lower metal mold.
(58) Desirably, the ratio of diameter of the molten resin mass to the diameter of the lower metal mold remains nearly the same so that the molten resin mass comes in contact as much as possible with the whole portion that is defining the bottom portion of the lower metal mold. This, however, differs depending on the shape of the metal mold. For instance, if the lower metal mold to which the molten resin mass is fed is of the type different from that of the female metal mold, it becomes probable that the molten resin mass may come into contact with a portion (side surface of the cavity) that defines the body portion. It is, therefore, desired that the ratio D2/D1 is in a range of 0.95 to 0.7. If the lower metal mold is of the type that becomes the male metal mold, there is no such limitation and, therefore, the ratio D2/D1 should desirably lie in a range of 1 to 0.7.
(59) Even in case the lower metal mold is the male metal mold having the core and the upper metal mold is the female metal mold having the cavity as shown in
(60) In the method of forming the cup-type container of the present invention, it is particularly desired that the molten resin mass which is in the molten state is a molten resin mass having a multi-layer structure extruded by a die head having a multi-layer structure. That is, the strand having the multi-layer structure extruded by the die head having the multi-layer structure is cut by a cutting means of a synthetic resin feeding apparatus. The molten resin mass that is cut is covered at its cutting end with the outer layer, and is formed into a molten resin mass having the multi-layer structure that includes a core layer located at the center and shell layers wrapping the core layer therein. Despite the molten resin mass having the above multi-layer structure is compression-formed, the intermediate layer is not exposed to the surface, and there is no need of taking into account the hygienic property of the resin used as the intermediate layer.
(61) For instance, if the desired cup-type container has a two-kind-three-layer multi-layer structure using the polypropylene as the inner and outer layers and using the barrier resin as the intermediate layer, the molten resin mass may comprise the core layer of the barrier resin and the shell layers of the polypropylene.
EXAMPLES
(62) The invention will be further described by way of the Examples.
(63) 1. Measuring the Half-Value Width at a Half Peak.
(64) (1) Measuring Apparatus and Measuring Conditions. Transmission Type Small X-Ray Diffraction
(65) apparatus RAD-RB (manufactured by Rigaku Co.)
(66) Target: Cu,
(67) Filter: Ni
(68) Detector: goniometer PSPC MDG
(69) Counting gas: Ar 90%+CH.sub.4 10%,
(70) Counting gas pressure: 180 kgf/cm.sup.2
(71) Voltage: 30 kV,
(72) Current: 90 mA,
(73) Scanning rate: 2°/min.
(74) Step width: 0.081°,
(75) Measuring time: 600 seconds
(76) (2) Calculating the Half-Value Width at a Half Peak by Measuring the X-Ray Diffraction Intensities.
(77) A test piece was cut out from the body portion of the cup-type container, and the direction of height thereof was denoted by x and the circumferential direction by y. By using the measuring apparatus mentioned above, the diffraction intensities were measured by causing an X-ray to be incident on a plane x-y of the test piece at right angles thereto.
(78) Here, in a peak intensity profile in the x-direction of a Debye's ring that was obtained, the half-value width at a half peak of Miller index was measured at a diffraction angle 2 θ=14.5° that represented the diffraction by the crystal plane (110). The number of the samples measured was N=3, and an average value thereof was regarded to be a measured result.
(79) Here, if a line is drawn in parallel with the abscissa passing through a point one-half the peak intensity of the Miller index at a diffraction angle 2θ=14.5° representing the diffraction by the crystal plane (110), the half-value width is the width between the two points at where the parallel line intersects the peak curve.
(80) In measuring the half-value width at a half peak, in order to exclude the effect of X-ray scattering caused by the air during the measurement, the air scattering value measured in the absence of the test piece was subtracted from the measured values to thereby find the half-value width at a half peak due purely the test piece only.
(81) The test piece was cut in a square shape having a side of 10 mm such that the height h of the cup-type container above the ground surface was the center of the test piece.
(82) The results were as shown in Table 1 and
(83) (3) Calculating the half-value width at a half peak and the rate of change in the half-value width in the bottom portion by measuring the X-ray diffraction intensities.
(84) A test piece was cut out from the bottom portion of the cup-type container, and the radial direction thereof was denoted by x and the circumferential direction by y. By using the measuring apparatus mentioned above, the diffraction intensities were measured by causing the X-ray to be incident on a plane x-y of the test piece at right angles thereto. The half-value width at a half peak was found by the same method as that of the case of the body portion.
(85) The results of the half-value widths at a half peak were as shown in Table 6(A), while the results of the rates of change K in the half-value widths at half peaks were as shown in Table 6(B) and
(86) 2. Evaluating the Heat Shrinkage.
(87) (1) Calculating the Heat Shrinkage in the Body Portion of the Cup-Type Container.
(88) By using an autoclave (SS-325 manufactured by Tommy Kogyo K.K.), a cup-type container was heated under the conditions of 95° C. for 30 minutes, and the fully poured capacities were measured before and after the heating to calculate the rate of change before and after the heating. The number of the samples was N=3, and an average value thereof was regarded to be the measured result.
(89) The results were as shown in Table 2 and
(90) (2) Calculating the Heat Shrinkage in the Bottom Portion of the Cup-Type Container.
(91) The bottom portion only was cut out from the cup-type container, heated under the above-mentioned conditions, and was measured for its thicknesses at four places of the radius ratios r/R of 0, 0.36, 0.72 and 0.9 before and after the heating to calculate the rates of change.
(92) The number of the samples measured was N=3, and an average value thereof was regarded to be the measured result. Here, at three places of the ratios r/R of 0.36, 0.72 and 0.9, the thicknesses were found by averaging the measurements at 8 points.
(93) The results were as shown in Table 7 and
(94) 3. Evaluating the Positions where the Intermediate Layer that Extended has Reached.
(95) A vicinity of the flange portion of the cup-type container was equally cut in 8 directions in parallel in the direction of height, and the cut surfaces were trimmed. Thereafter, an iodine solution was applied to dye the ethylene-vinyl alcohol copolymer resin of the intermediate layer. The cut surfaces were observed by using a graduated magnifying glass to measure the positions where the intermediate layer has reached. The number of the samples was N=3, and an average value thereof was regarded to be the measured result. By regarding the position 3a in
(96) The results were as shown in Table 3 and
(97) 4. Evaluating the Position of the Intermediate Layer in the Direction of Thickness.
(98) The cup-type container was cut in the direction of height from the flange toward the bottom portion, and the cut surfaces were trimmed. Thereafter, the iodine solution was applied to dye the ethylene-vinyl alcohol copolymer resin of the intermediate layer. The cut surfaces were observed by using a digital camera-incorporating stereoscopic microscope (LEICA EZ4 uD) (Leica Microsystems Co.) to measure t.sub.2 and t.sub.3 in
C=(t.sub.2+t.sub.3/2)/t (2)
(99) The results were as shown in Table 4 and
(100) 5. Evaluating the Oxygen-Barrier Property.
(101) The cup-type container was fully filled with water and was boiled and sterilized under a condition of 80° C.-30 minutes. Thereafter, the cup-type container was stored for a predetermined period of time in an environment of 30° C.-40±10% RH, and an oxygen concentration in the container was measured by using a CheckMate 9900 (PBI DANSENSOR Co.). The storage terms were 1, 14 and 30 days. The number of the samples was N=5, and an average value thereof was regarded as the measured results.
(102) The results were as shown in Table 5 and
(103) 6. Evaluating the Shatter Strength.
(104) The cup-type container was fully filled with water, heat-sealed with a lid member and was, thereafter, stored for one day in an environment of a temperature of 23° C. and a humidity of 50%. Thereafter, with the bottom facing downward, the container was allowed to fall down one time from a height of 50 cm. The container, when it was not shattered, was caused again to fall down from a height of 80 cm. The shatter strength was evaluated based on the height the container was shattered. Here, the container was shattered means that the water filled in the container has leaked.
(105) The results were as shown in Table 8 and
Example 1
(106) A random polypropylene resin (MFR 30 g/10 min) was fed into a φ65 extruder (L/D=30), extruded through a nozzle of an outlet diameter of φ27 under the conditions of an extruder temperature of 230° C., die temperature of 230° C. and a resin pressure of 9.0 MPa, and was cut to obtain a molten resin mass. The molten resin mass was fed into a compression metal mold maintained at 18° C., compression-formed while defining, in advance, part of the flange, varying the thicknesses of the body portion of the container and of the portion that forms the bottom and controlling the forming rate to be 100 mm/sec at a point 5 mm before the point where the forming was completed to thereby obtain a single-layer cup-type container of a sectional structure as shown in
(107) Next, the single-layer cup-type container was found for its half-value width at a half peak to evaluate its heat shrinkage.
Example 2
(108) As a resin for forming inner and outer layers, a random polypropylene resin (MFR 30 g/10 min) was fed into the φ65 extruder (L/D=30), and was extruded under the conditions of an extruder temperature of 230° C. and a resin pressure of 9.0 MPa.
(109) Further, an ethylene-vinyl alcohol copolymer resin was fed into a φ30 extruder (L/D=25) and was extruded under the conditions of an extruder temperature of 230° C. and a resin pressure of 30.0 MPa.
(110) As an adhesive resin for adhering the intermediate layer to the inner and outer layers, further, a modified polypropylene resin was fed into a φ30 extruder (L/D=25) and was extruded under the conditions of an extruder temperature of 230° C. and a resin pressure of 22.0 MPa.
(111) The inner and outer layers, intermediate layer and adhesive resin were met together in a die heated at 230° C., extruded through a nozzle of an outlet diameter of φ27, and was cut to obtain a multi-layer molten resin mass.
(112) The multi-layer molten resin mass was compression-formed under the same conditions as in Example 1 to obtain a multi-layer cup-type container of the same shape as that of Example 1 and having a constitution in which the inner and outer layers were formed of the random polypropylene resin, the intermediate layer was formed of the ethylene-vinyl alcohol copolymer resin, and the adhesive layers among the inner and outer layers and the intermediate layer were formed of the modified polypropylene resin.
(113) Next, the multi-layer cup-type container was found for its half-value width at a half peak to evaluate its heat shrinkage and the position to where the intermediate layer has extended.
Example 3
(114) A random polypropylene resin (MFR 22 g/10 min) was fed into a φ75 extruder (L/D=30), extruded through a nozzle of an outlet diameter of φ27 under the conditions of an extruder temperature of 220° C., a die temperature of 220° C. and a resin pressure of 1.2 MPa, and was cut to obtain a molten resin mass. The molten resin mass was compression-formed under the same forming conditions as those of Example 1 except that the temperature was 20° C. in the compression metal mold to which the molten resin mass was fed, and the forming rate was 300 mm/sec at a point 5 mm before the point where the forming was completed. There was obtained a single-layer cup-type container of the same shape as that of Example 1, which was then measured and evaluated in the same manner as in Example 1.
Example 4
(115) By using the random polypropylene resin (MFR 22 g/10 min), there was obtained a molten resin mass in the same manner as in Example 3. The molten resin mass was compression-formed under the same forming conditions as those of Example 1 (specifically, the forming rate was 100 mm/sec at a point 5 mm before the point where the forming was completed) except that the temperature was 20° C. in the compression metal mold to which the molten resin mass was fed. There was obtained a single-layer cup-type container of the same shape as that of Example 1, which was then measured and evaluated in the same manner as in Example 1.
Example 5
(116) As a resin for forming inner and outer layers, the random polypropylene resin (MFR 22 g/10 min) was fed into a φ75 extruder (L/D=30), and was extruded under the conditions of an extruder temperature of 220° C. and a resin pressure of 1.2 MPa.
(117) Further, an ethylene-vinyl alcohol copolymer resin was fed into a φ25 extruder (L/D=25) and was extruded under the conditions of an extruder temperature of 220° C. and a resin pressure of 2 MPa.
(118) As an adhesive resin for adhering the intermediate layer to the inner and outer layers, further, a modified polypropylene resin was fed into the φ30 extruder (L/D=25) and was extruded under the conditions of an extruder temperature of 220° C. and a resin pressure of 4.8 MPa.
(119) The inner and outer layers, intermediate layer and adhesive resin were met together in a die heated at 230° C., and was cut to obtain a multi-layer molten resin mass.
(120) The multi-layer molten resin mass was compression-formed under the same conditions as in Example 3 except that the forming rate was 130 mm/sec at a point 5 mm before the point where the forming was completed to obtain a multi-layer cup-type container of the same shape as that of Example 1 and having a constitution in which the inner and outer layers were formed of the random polypropylene resin, the intermediate layer was formed of the ethylene-vinyl alcohol copolymer resin, and the adhesive layers among the inner and outer layers and the intermediate layer were formed of the modified polypropylene resin. Next, the multi-layer cup-type container was evaluated for its position to where the intermediate layer has extended.
Example 6
(121) A multi-layer molten resin mass was obtained in the same manner as in Example 5 and was compression-formed under the same forming conditions as in Example 3 except that the forming rate was 40 mm/sec at a point 5 mm before the point where the forming was completed to obtain a multi-layer cup-type container of the same shape as that of Example 5. Next, the multi-layer cup-type container was evaluated in the same manner as in Example 5.
Example 7
(122) A random polypropylene resin (MFR 10 g/10 min) was used and was extruded through a nozzle of an outlet diameter of φ27 under the same conditions as those of Example 3, and was cut to obtain a molten resin mass. The molten resin mass was compression-formed under the same conditions as those of Example 6 to obtain a single-layer cup-type container having the same shape as that of Example 1 and weighing 11 g. Next, the single-layer cup-type container was measured and evaluated in the same manner as in Example 1.
Example 8
(123) A random polypropylene resin (MFR 22 g/10 min) was used and was extruded through a nozzle of an outlet diameter of φ32 under the same conditions as those of Example 3, and was cut to obtain a molten resin mass. The molten resin mass was compression-formed under the same conditions as those of Example 6 to obtain a single-layer cup-type container having a sectional structure as shown in
Comparative Example 1
(124) A commercially available polypropylene multi-layer injection-formed cup-type container having the same shape as that of Example 1 and having inner and outer layers of a random polypropylene resin, was measured and evaluated in the same manner as in Example 2.
Comparative Example 2
(125) A commercially available homopolypropylene multi-layer pressure-formed cup-type container having the sectional structure as shown in
Comparative Example 3
(126) A random polypropylene resin (MFR 22 g/10 min) was fed into a φ75 extruder (L/D=30), extruded under the conditions of an extruder temperature of 220° C., a die temperature of 220° C. and a resin pressure of 1.2 MPa, and was cut to obtain a molten resin mass. The molten resin mass was compression-formed under the conditions same as those of Example 3 to obtain a single-layer cup-type container having the sectional structure as shown in
Comparative Example 4
(127) A random polypropylene resin (MFR 10 g/10 min) was used and was extruded through a nozzle of an outlet diameter of φ20 under the same conditions as those of Example 3, and was cut to obtain a molten resin mass. The molten resin mass was compression-formed under the same conditions as those of Example 3 to obtain a single-layer cup-type container having the same shape as that of Example 3. Next, the single-layer cup-type container was measured and evaluated in the same manner as in Example 1.
(128) [Experiment]
(129) There were pressure-formed polypropylene multi-layer cup-type containers having a container flange outer diameter of 75 mm and a capacity of 100 cc while varying the inner layer/outer layer ratio at the position of the intermediate layer in cross section of the container as shown in Table 5. The oxygen concentrations in the containers were evaluated depending on the respective inner layer/outer layer ratios.
(130) In the cup-type containers, the inner and outer layers were formed by using the polypropylene resin, the intermediate layer was formed by using the ethylene-vinyl alcohol copolymer resin, and the adhesive layers among the inner and outer layers and the intermediate layer were formed by using the modified polypropylene resin. The thickness of the intermediate layer was maintained constant in all of these containers.
(131) In Table 1 below, the half-value width of the main body portion at various heights from the ground surface are provided for listed examples.
(132) TABLE-US-00001 TABLE 1 Half-value Height from the ground surface [mm] width 10 25 40 45 70 Example 1 1.37 — 1.34 — 1.35 Example 2 1.34 — 1.34 — 1.41 Example 3 1.33 — 1.28 — 1.34 Example 4 1.35 — 1.29 — 1.36 Comp. Ex. 1 1.17 — 1.16 — 1.18 Comp. Ex. 2 1.09 — 0.90 — 0.91 Comp. Ex. 3 1.09 1.26 — 1.32 —
(133) TABLE-US-00002 TABLE 2 Rate of change in full capacity before and Rate of change after the heating [%] Example 1 −1.03 Example 2 −1.00 Example 3 −1.00 Example 4 −1.27 Comp. Ex. 1 −1.54 Comp. Ex. 2 −3.86 Comp. Ex. 3 −1.88
(134) TABLE-US-00003 TABLE 3 Position to where the intermediate layer has Direction of measurement extended [mm] 1 2 3 4 5 6 7 8 Average Example 5 −7.2 +2.7 −4.2 −10.5 −11.8 −15.3 −9.9 −6.8 −7.9 Example 6 +4.2 +6.3 +6.0 +8.0 +4.5 +2.3 +4.5 +2.6 +4.8
(135) TABLE-US-00004 TABLE 4 Inner layer thickness ratio C of container Distance from the center of the bottom [mm] barrier layer 10 25 45 65 85 105 115 Example 2 0.58 0.46 0.46 0.42 0.38 0.38 — Example 5 0.57 0.48 0.35 0.29 0.29 0.32 — Example 6 0.54 0.43 0.36 0.32 0.30 0.36 0.56 Comp. Ex. 1 0.15 0.16 0.22 0.24 0.27 0.36 0.58
(136) TABLE-US-00005 TABLE 5 Oxygen concentration in the container depending on inner/outer layer ratio of the container Inner layer/outer layer ratio of the container Days of storage (inner:outer) 1 Day 14 Days 30 Days 75:25 0.03% 0.10% 0.19% 70:30 0.03% 0.10% 0.19% 60:40 0.02% 0.11% 0.20% 50:50 0.03% 0.13% 0.25% 40:60 0.03% 0.22% 0.47% 30:70 0.05% 0.52% 1.01% 25:75 0.06% 0.67% 1.48%
(137) TABLE-US-00006 TABLE 6 (A) Radius ratio r/R from the Half-value width in center of the bottom the bottom portion 0 0.36 0.72 Example 1 1.30 1.31 1.30 Example 2 1.35 1.32 1.34 Example 7 1.32 1.28 1.26 Example 8 1.39 1.40 1.38 Comp. Example 1 1.27 1.22 1.19 Comp. Example 2 1.09 1.00 1.02 Comp. Example 4 1.31 1.15 0.99 (B) Rate of change of Radius ratio r/R from the half-value width in center of the bottom the bottom portion 0 0.36 0.72 Example 1 1.00 1.01 1.00 Example 2 1.00 0.98 0.99 Example 7 1.00 0.97 0.95 Example 8 1.00 1.01 0.99 Comp. Example 1 1.00 0.96 0.93 Comp. Example 2 1.00 0.92 0.93 Comp. Example 4 1.00 0.88 0.76
(138) TABLE-US-00007 TABLE 7 Radius ratio r/R from the Rate of change of thickness center of the bottom before and after the heating 0 0.36 0.72 0.90 Example 1 +0.205 +0.383 −0.133 −0.358 Example 2 +1.114 +1.222 +1.024 +0.697 Example 7 +1.385 +0.708 +1.316 +1.229 Comp. Ex. 4 +2.386 +1.930 +2.392 +3.078
(139) TABLE-US-00008 TABLE 8 Shattered Falling height, 50 mm Falling height, 80 mm container Number Shattering Number Shattering bottom shattered/ rate shattered/ rate portion total number [%] total number [%] Example 7 1/30 3.33 3/29 10.34 Comp. Ex. 4 1/30 3.33 5/29 17.24
(Consideration)
(140) In the case of the cup-type container having L/D which is not so large but is about 1.0 as shown in
(141) In Examples 2, 5 and 6, the molten resins are compression-formed and the intermediate layer is present in nearly the middle of the container near the bottom. As the fluidizing distance increases, however, the molten resin deviates toward the inner surface side. Near the flange, the molten resin flows again toward the outer surface. As a whole, therefore, the intermediate layer is present at a position of an inner layer thickness ratio of 0.3 to 0.5. By controlling the position of the resin of the intermediate layer in a state of the molten resin mass of before the compression forming, further, it is allowed to control the position of the intermediate layer to some extent in the cup-type container after it has been formed.
(142) In Comparative Example 1, on the other hand, the molten resin is injection-formed and, therefore, the intermediate layer injected from the gate is present at a position very close to the inner surface near the bottom. The resin as it further flows tends to approach the outer surface. As a whole, therefore, the inner layer thickness ratio assumes a value of not larger than 0.5.
(143) As the intermediate layer becomes closer to the inner surface, it will be learned that the oxygen-barrier property decreases being affected by the water of the content. Considering from the results of the inner layer thickness ratios C, the cup-type container injection-formed like in Comparative Example 1 has the intermediate layer that is close to the inner surface. Being affected by the water of the content, therefore, the oxygen-barrier property of the intermediate layer decreases. On the other hand, the cup-type containers compression-formed as in Examples 2, 5 and 6 have an intermediate layer positioned more away from the inner surface than in Comparative Example 1. Therefore, it is considered that the intermediate layer is less affected by the water of the content and permits the oxygen-barrier property to decrease little.
(144) From
(145) Referring to
(146) As will be obvious from
INDUSTRIAL APPLICABILITY
(147) Owing to its excellent mechanical strengths such as heat resistance and shatter strength of the bottom portion as well as excellent transparency and gas-barrier property, the cup-type container of the invention can be favorably used for containing, specifically, beverages and foods.
(148) Moreover, the cup-type container features excellent dimensional precision and forms a thick stacking portion. Therefore, the cup-type containers of the invention can be stacked one upon the other in a plural number, and can be effectively used for containing general-purpose products that are mass-produced.
DESCRIPTION OF REFERENCE NUMERALS
(149) 1: body portion 2: bottom portion 3: flange portion 4: stacking portion 5: leg portion 6: intermediate layer 7: inner layer 8: outer layer 9: body portion 11: lower metal mold (female mold) 12: upper metal mold (male mold) 13: metal mold for defining flange-forming space 14: space for forming bottom portion 15: space for forming body portion 16: space for forming product flange portion 17: molten resin mass 18: ground surface on where the product is erected