GB2111908A - Thermoplastic resin laminate for vacuum forming - Google Patents
Thermoplastic resin laminate for vacuum forming Download PDFInfo
- Publication number
- GB2111908A GB2111908A GB08231298A GB8231298A GB2111908A GB 2111908 A GB2111908 A GB 2111908A GB 08231298 A GB08231298 A GB 08231298A GB 8231298 A GB8231298 A GB 8231298A GB 2111908 A GB2111908 A GB 2111908A
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- thickness
- film
- laminate
- laminates
- thermoplastic resin
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Classifications
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B32—LAYERED PRODUCTS
- B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
- B32B27/00—Layered products comprising a layer of synthetic resin
- B32B27/06—Layered products comprising a layer of synthetic resin as the main or only constituent of a layer, which is next to another layer of the same or of a different material
- B32B27/08—Layered products comprising a layer of synthetic resin as the main or only constituent of a layer, which is next to another layer of the same or of a different material of synthetic resin
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C51/00—Shaping by thermoforming, i.e. shaping sheets or sheet like preforms after heating, e.g. shaping sheets in matched moulds or by deep-drawing; Apparatus therefor
- B29C51/14—Shaping by thermoforming, i.e. shaping sheets or sheet like preforms after heating, e.g. shaping sheets in matched moulds or by deep-drawing; Apparatus therefor using multilayered preforms or sheets
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B32—LAYERED PRODUCTS
- B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
- B32B27/00—Layered products comprising a layer of synthetic resin
- B32B27/30—Layered products comprising a layer of synthetic resin comprising vinyl (co)polymers; comprising acrylic (co)polymers
- B32B27/302—Layered products comprising a layer of synthetic resin comprising vinyl (co)polymers; comprising acrylic (co)polymers comprising aromatic vinyl (co)polymers, e.g. styrenic (co)polymers
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B32—LAYERED PRODUCTS
- B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
- B32B27/00—Layered products comprising a layer of synthetic resin
- B32B27/30—Layered products comprising a layer of synthetic resin comprising vinyl (co)polymers; comprising acrylic (co)polymers
- B32B27/304—Layered products comprising a layer of synthetic resin comprising vinyl (co)polymers; comprising acrylic (co)polymers comprising vinyl halide (co)polymers, e.g. PVC, PVDC, PVF, PVDF
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B32—LAYERED PRODUCTS
- B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
- B32B27/00—Layered products comprising a layer of synthetic resin
- B32B27/32—Layered products comprising a layer of synthetic resin comprising polyolefins
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B32—LAYERED PRODUCTS
- B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
- B32B27/00—Layered products comprising a layer of synthetic resin
- B32B27/36—Layered products comprising a layer of synthetic resin comprising polyesters
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B32—LAYERED PRODUCTS
- B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
- B32B38/00—Ancillary operations in connection with laminating processes
- B32B38/0012—Mechanical treatment, e.g. roughening, deforming, stretching
- B32B2038/0028—Stretching, elongating
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B32—LAYERED PRODUCTS
- B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
- B32B2250/00—Layers arrangement
- B32B2250/24—All layers being polymeric
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B32—LAYERED PRODUCTS
- B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
- B32B2309/00—Parameters for the laminating or treatment process; Apparatus details
- B32B2309/60—In a particular environment
- B32B2309/68—Vacuum
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B32—LAYERED PRODUCTS
- B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
- B32B2323/00—Polyalkenes
- B32B2323/04—Polyethylene
- B32B2323/043—HDPE, i.e. high density polyethylene
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B32—LAYERED PRODUCTS
- B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
- B32B2323/00—Polyalkenes
- B32B2323/04—Polyethylene
- B32B2323/046—LDPE, i.e. low density polyethylene
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B32—LAYERED PRODUCTS
- B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
- B32B2323/00—Polyalkenes
- B32B2323/10—Polypropylene
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B32—LAYERED PRODUCTS
- B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
- B32B2325/00—Polymers of vinyl-aromatic compounds, e.g. polystyrene
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B32—LAYERED PRODUCTS
- B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
- B32B2327/00—Polyvinylhalogenides
- B32B2327/06—PVC, i.e. polyvinylchloride
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B32—LAYERED PRODUCTS
- B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
- B32B2367/00—Polyesters, e.g. PET, i.e. polyethylene terephthalate
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B32—LAYERED PRODUCTS
- B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
- B32B2439/00—Containers; Receptacles
- B32B2439/70—Food packaging
Landscapes
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- Laminated Bodies (AREA)
- Blow-Moulding Or Thermoforming Of Plastics Or The Like (AREA)
- Addition Polymer Or Copolymer, Post-Treatments, Or Chemical Modifications (AREA)
- Shaping By String And By Release Of Stress In Plastics And The Like (AREA)
- Manufacture Of Macromolecular Shaped Articles (AREA)
Abstract
A structure of a stretched thermoplastic resin film laminated upon an unstretched thermoplastic resin sheet, the structure having a thickness proportion of the film based on the laminated structure of 1.0 to 20%, and being useful in vacuum forming, the sheet being preferably of a polyolefin resin and the film being preferably of a polyolefin resin and prepared by stretching in a draw ratio of 4 times or greater.
Description
SPECIFICATION
Thermoplastic resin laminate for vacuum forming
BACKGROUND OF THE INVENTION
Field of the invention
This invention relates to a thermoplastic resin laminate for vacuum forming. More particularly it relates to a thermoplastic resin laminate having an improved vacuum-formability, obtained by laminating a stretched thermoplastic resin film upon an unstretched thermoplastic resin sheet.
Description of the prior art
Thermoplastic resin sheets have been used as stocks for producing containers for foods, etc. or other molded products according to forming processes such as vacuum forming, air-pressure forming, etc.
Among thermoplastic sheets, those comprising polyolefin resins, particularly polypropylene resins, are inferior to those comprising rigid vinyl chloride polymer resins or polystyrene in the point of processability for secondary processing such as vacuum forming or air-pressure forming (both the formings will hereinafter be collectively referred to as vacuum forming, etc.). As processes for overcoming such a drawback inherent to polypropylene resin (hereinafter abbreviated to polypropylene), the following improved processes are known: In the production of the sheets, polypropylene having a small MFR (melt flow rate) is used or a low density polyethylene (hereinafter abbreviated to LDPE) or a high density polyethylene (hereinafter abbreviated to HDPE) is blended to polypropylene.However, when such improvements are brought into practice, the processabilities in vacuum forming, etc. (hereinafter referred to as formability in vacuum forming, etc.) are improved to a certain extent, but on the other hand, other drawbacks such as lowering of transparency, rigidity and other physical properties of the resulting molded products are brought about.
On the other hand, lamination of thermoplastic resin films of the same or different properties upon one another has been widely carried out. Examples of such laminates practically used include mainly cellophane and LDPE film (designated also as "cellophane/LDPE film"; such designation being applied to the succeeding examples), biaxially stretched polypropylene film (hereinafter abbreviated to OPP)/LDPE film and OPP/unstretched polypropylene film (hereinafter abbreviated to CPP), and the object of such lamination is to improve characteristic properties of these films such as heat-sealability, moisture resistance, airtight property, etc. As seen from such object, the uses of these laminated films have been directed to packaging materials or the like.Further, the respective thickness of these laminated films are about 30 11 or less; hence such laminated films are different from the laminates of the present invention mentioned later in the thickness.
The present inventors have made earnest studies to overcome the above-mentioned drawbacks occurring when the thermoplastic resin sheets, particularly polyolefin resin sheets, above all polypropylene resin sheets are used in vacuum forming, etc., by way of processes different from the above-mentioned conventional ones. As a result, it has been found that the above-mentioned drawbacks (including new drawback accompanying the prior art) can be overcome by laminating a definite stretched thermoplastic resin film upon an unstretched thermoplastic resin sheet.
As apparent from the foregoing, the object of the present invention is to provide a thermoplastic resin laminated sheet having new uses. Another object is to provide molded products having superior physical properties and obtained by subjecting the above laminated sheet to secondary processing according to vacuum forming, etc. Other objects will be apparent from the following description.
Summary of the invention
The present invention resides in:
(1) A structure of a stretched thermoplastic resin film laminated upon an unstretched thermoplastic resin sheet, having a thickness proportion of said stretched thermoplastic resin film based on said structure of 1.0 to 20%, which structure is useful for vacuum forming (this structure will hereinafter be referred to as laminate);
(2) a laminate of the above-mentioned item (1 ) wherein said unstretched thermoplastic resin sheet comprises a polyolefin resin; and
(3) a laminate of the above-mentioned item (1 ) wherein said stretched thermoplastic resin film comprises a polyolefin resin and is prepared in a draw ratio of 4 times or greater.
Brief description of the drawings
Figure 1A, Figure 1B and Figure 1C show relationships between heating behaviors (sagging quantity, recovered quantity and retention time) of the laminates of the present invention and proportions of the thickness of stretched films.
Figure 2A, Figure 2B and Figure 2C show relationships between physical properties (haze, Young's modulus and impact strength) of the laminates of the present invention and proportions of the thickness of stretched films.
Detailed description of the invention
The constitutional elements and effectiveness of the present invention will be described below in detail.
(a) Unstretched thermoplastic resin sheet:
Thermoplastic resins used may be those which can be processed into sheets and further can be used for secondary processing, and examples of these are polyolefin resins such as LDPE, HDPE, polypropylene, polybutene-1, poly-4-methylpentene-1 and further, vinyl chloride polymer resins, polystyrene, polyester resins, etc. These resins include not only homopolymers, but also copolymers of monomers of the same or different kinds (random copolymers, block copolymers and graft copolymers). Further, not only polymers of one kind but also blends of polymers of two or more kinds can be used. Necessary stabilizers and besides, various fillers, pigments and additives can be, of course, added to these resins.
The sheets are prepared according to any one of processes, i.e. any of these such as calendering process,
T-die process, roll uniaxial stretching process, etc. may be employed. The thickness of the sheets is in the range of 100 to 2,000 Il, preferably 200 to 1,000 Il. If the thickness is less than 100 Il, the sheets are unsuitable as materials for vacuum forming, etc. and if it exceeds 2,000 CL, other processing techniques such as press forming will be more suitable.
(b) Stretched thermoplastic film:
Thermoplastic resins used are the same as in the case of the thermoplastic resins described in the above item (a). The preparation of the film also is the same as in the above-mentioned sheet except for the thickness after stretching. Namely, the film has a thickness in the range of 5 to 50 , preferably 10 to 30 and is prepred by stretching to 4 times or more (surface draw ratio). If the draw ratio is less than 4 times, the effectiveness of the present invention described later is very insufficient.Although the upper limit of the draw ratio is not limited, about 60 times are a limitative draw ratio in view of the current processing techniques, and even if a film obtained by stretching in a draw ratio exceeding the above value is used, the effectiveness of the present invention is not particularly enhanced. Any of known stretching processes may be employed such as tenter biaxial stretching process, inflation multi-axial stretching process, roll uniaxial stretching process, etc. Further, either of uniaxially stretched product or multi-axially stretched product can, of course, be used.
The sheet and the film prepared as described above are laminated according to any of known processes.
As to such lamination processes, any of known extrusion lamination processes, dry lamination process and others may be employed. However, extrusion lamination process is preferred in view of the production efficiency and the quality of the resulting laminate of the present invention. If the respective thermoplastic resins of the sheet and the film of the present invention are of the same kind, the sheet and the film are generally easily melt-adhered together, but if they are of different kinds, they are not always melt-adhered together; hence in such a case, the sheet and the film are adhered together by an adhesive.
(d) Proportion of the thickness of the stretched thermoplastic resin film based on that of the resulting laminate:
The proportion of the thickness of the film constituting the laminate of the present invention based on that of the laminate must be in the range of 1.0 to 20%, preferably 3 to 15%. If it exceeds 20%, broken parts occur in the resulting laminate at the time of vacuum forming, etc. due to the loosening of orientation of the laminated stretched film, resulting in failure of vacuum forming, etc. Contrarily if the proportion is less than 1.0%, various effects brought about by the lamination of the stretched film (improvements in vacuum forming process, rigidity and impact strength) are notably decreased; hence the object of the present invention practically cannot be attained.
By carrying out vacuum forming, etc. by the use of the laminate of the present invention as described above in detail, it has now become possible to realize the following various effects: (1) As to thermoplastic resins as raw material, it is unnecessary to use particularly those having a lower
MFR.
(2) In the case of polypropylene resin, it is unnecessary to mix it with another kind of resin.
(3) Formability in vacuum forming, etc., expressed by heating behaviours (see Examples) is improved.
(4) Transparency of the resulting molded product is improved to a large extent.
(5) Rigidity (Young's modulus) and impact strength of the resulting molded product are improved.
Heating behaviours are measured as follows:
A laminate sample is fixed onto a frame having an opening part of 300 x 300 mm, and the thus fixed laminate is maintained horizontallyfora definite period oftime in a heating oven maintained at 1800C. By this heating, a central portion of the laminate first sags, thereafter the original state is partially recovered from such a sagging and such a recovered state continues for a definite period of time. The term "sagging quantity" referred to in the following Examples means the largest sagging quantity (mm) prior to initiating the above-mentioned partial recovery; the term "recovered quantity" means a percentage recover (%) in the state where the largest recovery occurred; and the term "retention time" means a period of time (sec.) for which the largest recovered quantity is maintained. The above-mentioned recovered state is lost by resagging which occurs after lapse of the retention time, and thereafter such a recovery phenomenon does not occur.
The present invention will be described by way of Examples.
Examples 1- 14 and Comparative examples 1 and 2 A commercially available polypropylene resin having a MFR of 3.3 (Chissopolypro A5014, trade name of product manufactured by Chisso Corportion) was extruded through a T-die of 75 mmQ established at a temperature of 250 C, and at that time, onto the resulting extruded sheet was laminated each of OPPs of 12, 18,20 and 30 C1 thick (draw ratio, 40 times; Examples 1 - 12), an inflation process, multi-axially stretched polypropylene film of 20 y thick (hereinafter abbreviated to IOPP; draw ratio, 36 times; Example 13) and a uniaxially stretched polypropylene film of 20 thick (draw ratio, 8 times;Example 14), separately prepared, respectively, and the thickness of the unstretched part at the time of the extrusion was also adjusted to obtain laminates having respectively a thickness after the lamination of 250 u (Examples 1 - 4), that of 350 u (Examples 5 - 8, 13 and 14) and that of 500 CL (Examples 9 - 12). Further, as Comparative examples, laminates of CPP of 20 thick onto the extruded sheet (Comparative example 1) and a non-laminated sheet (Comparative example 2), each having a total thickness of 350 U, were prepared.The constitutions and physical properties of these laminates and the sheet are shown in Table 1 and the respective relationships between various physical properties and the proportions of the thickness of the laminated stretched films are shown in Figure 1 and Figure 2. The relationships between heating behaviours (sagging quantity, recovered quantity and retention time) and vacuum-formability will be described below. Figure 1A, Figure 1 B and
Figure 1 C show the relationships between sagging quantity, recovered quantity and retention time among the heat behaviours of the laminates of the present invention and proportions of the thickness of stretched films. The curves in these Figures are obtained by plotting the respective heating behaviours of each sample having the same thickness against the thickness proportions.In Figures 1A, 1 B and 1 C, symbols A, A and 0 show measurement results of laminates of OPP having a thickness of 500 U' 350 U and 250 y, of the present invention, respectively, and symbols x and [ show those of laminates of IOPP and monoaxially stretched polypropylene film, respectively. As apparent from Figure 1A, as to the sagging quantity, laminates having a larger total thickness are superior with regard to those having the same thickness proportions, but with regard to the same thicknesses of laminates, preferred results are obtained in thickness proportions of 2% or higher, particularly about 4% or higher.As apparent from Figure 1 B, as to the recovered quantity, preferred results (close to 100%) are obtained in thickness proportions of 2% or higher, particularly 3% or higher, with regard to laminates having the same thickness proportions, indifferently from the total thickness of laminates. As apparent from Figure 1 C, as to the retention time, laminates having a larger total thickness are superior with regard to those having the same thickness proportion, but with regard to the same thickness of laminates, preferred results are obtained in thickness proportions of 2% or higher, particularly 4% or higher.
As apparent from the above description of the measurement items of heating behaviors, the laminates for vacuum forming, etc. are superior in the formability in vacuum forming, etc. with the decrease of the sagging quantity, with the increase of the recovered quantity and with the increase of the retention time. Three upward arrow marks at the right ends of the three curves in Figure 1C means "values indicated there or higher". Further, it goes without saying that the physical properties of the laminates, as they are, show processability or physical properties attained after forming.
Next, Figure 2A, Figure 2B and Figure 2C show curves obtained by plotting the transparency (haze, %), the rigidity (Young's modulus, Kg)mm2) and the impact strength (Kg-cm) of the same samples as in Figure 1A,
Figure 1 B and Figure 1 C, respectively against the thickness proportions of the stretched films in the laminates of the present invention. In Figures 2A, 2B and 2C, symbols A, and 0 show measurement results of laminates of OPP having a thickness of 500 , a thickness of 350 U and a thickness of 250 U respectively, and symbols x and 2 show measurement results of laminate of IOPP (an inflation process multi-axially stretched film) and a laminate of uniaxially stretched polypropylene film, respectively.As apparent from Figure 2A, as to haze, laminates having a smaller total thickness are superior with regard to the same thickness proportions, but with regard to the same thickness of laminats, preferred results are obtained in thickness proportions of 2% or higher, particularly 3% or higher. On the other hand, lamintes of uniaxially stretched polypropylene or IOPP in place of OPP, having a thickness proportion of 5.7%, also have almost the same haze values as those of laminates of OPP, and the values are improved as a whole, down to about 2/3 to 1/2 of those in the case of no lamination (0%).As apparent from Figure 28, as to Young's modulus, laminates having a larger total thickness are superior with regard to the same thickness proportions, but with regard to the same thickness of laminates, preferred results are obtained in thickness proportions of 2% or higher, particularly about 5% or higher. On the other hand, laminates of uniaxially stretched polypropylene or IOPP in place of OPP, having a thickness proportion of 5.7% are considerably inferior to the corresponding laminates of OPP, differently from the case of haze (Figure 2A), but they are superior to a sheet of no lamination (0%) in the results. Further, as apparent from Figure 2C, as to impact strength, laminates having a larger total thickness are naturally superior with regard to the same thickness proportion, and preferred results are obtained in thickness proportions of 2% or higher, particularly about 4% or higher. On the other hand, laminates of uniaxially stretched polypropylene or IOPP in place of OPP, having a thickness proportion of 5.7%, are inferior to the corresponding laminates of OPP to a sheet of no lamination in the results. In addition, the laminates of CPP of Comparative example 1 exhibits no effectiveness except for improvement in transparency.
TABLE
Example Unit 1 2 3 4 5 6 7 8 Total thickness 256 350 of laminate Thickness of OPP 12 18 20 30 12 18 20 30 Thickness of IOPP Thickness of uniaxi- ally stretched film Thickness of CPP Thickness of proportion of film based on % 4.8 7.2 8.0 12 8.4 5.1 5.7 8.6 laminate Haze * % 16 15 15 14 24 22 22 21 Young's modulus ** Kg/mm 117 120 121 131 115 119 120 126 Impact strength *** KG-cm 6.2 9.0 9.4 13.1 8.6 12.7 13.0 17.5 Sagging quantity mm 30 26 27 23 29 27 27 24 Recovered quantity % 100 100 100 100 98 100 100 100 Retention time sec. 11 13 14 15 or 10 12 14 16 or longer longer TABLE 1 (continued)
Example Comparative Unit example 9 10 11 12 13 14 1 2**** Total thickness 500 350 350 350 350 of laminate Thickness of OPP 12 18 20 30 Thickness of IOPP 20 Thickness of uniaxi- 20 ally stretched film Thickness of CPP 20 Thickness of proportion of film based on % 2.4 3.6 4.0 6.0 5.7 5.7 5.7 0 laminate Haze * % 29 26 26 25 23 25 28 37 Young's modulus ** Kg/mm 115 118 119 123 116 114 108 112 Impact strength *** KG-cm 12.8 14.5 15.2 19.4 11.2 9.3 7.4 7.3 Sagging quantity mm 30 28 27 25 27 30 40 38 Recovered quantity % 98 98 98 100 100 98 61 63 Retention time sec. 10 12 13 15 or 13 16 4 5 longer Notes: *ASTM D-1003, **ASTM-882, ***ASTM D-781 (These apply to Tables 2 end 3.) **** non-laminated Examples 15 and 16 and Comparative examples 3-6
Unstretched sheets were prepared as in Examples 1 - 14, using a commercially available polypropylene resin having a MFR of 0.5 (Chissopolypro K 4011, tradename of product manufactured by Chisso
Corporation), a commercially available ethylene-propylene block copolymer resin having an ethylene content of 8% (Chissopolypro K701 1, tradename of product manufactured by Chisso Corporation) and a commercially available ethylene-propylene random copolymer resin having a MFR of 0.5 and an ethylene content of 3% (Chissopolypro XK 0235, tradename of product manufactured by Chisso Corporation), respectively, and at that time, OPP of 12 Uwas laminated upon the respective unstretched sheets to obtain laminates of 350 F (Examples 15 and 16). For comparison, sheets of 350 U having no OPP laminated were prepared (Comparative examples 3 - 5), and further, for comparison with the respective above Examples, a sheet of 3501l having no OPP laminated was prepared using a blend of the polypropylene resin with 10% by weight of LDPE having a melt index (MI) of 2.0 and 5% by weight of an ethylene-propylene rubber (Comparative example 6). The constitutions and physical properties of the above laminates and sheets are shown in Table 2.When the Examples are compared with the Comparative examples corresponding thereto (Example 15 to Comparative ex. 3; Example 16 to Comparative ex. 5; and Examples 15 - 17 to Comparative ex. 6), it is apparent that the laminates of the above Examples are superior to the sheets of the above
Comparative examples, in heating behaviors, transparency, rigidity and impact strength.
TABLE 2
Unit Example Comparative example
15 16 17 3 4 5 6
Raw Type of polymer Homo Block Random Homo Block Random Homo material g/
10min. 0.5 0.5 0.5 0.5 0.5 0.5 0.5
Thickness of OPP 12 12 12 - - -
Constitution Total thickness 350 350 350 350 350 350 350 of laminate of laminate or sheet
Thickness proportion
of OPP based on % 3.4 3.4 3.4 - - -
laminate
Haze % 32 48 27 55 80 51 82
Young's module Kg/mm 96 94 78 92 88 75 85
Impact strength Kg-cm 12 30 < 23 9 28 18 27
Sagging quantity mm 24 23 26 33 33 34 28
Heating Recovered quantity % 100 100 100 80 82 81 98
Behaviors Retention time sec. 13 14 14 7 8 7 20 Examples 18 and 19 and Comparative examples 7 and 8
Unstretched sheets were prepared as in Examples 1 - 14, using HDPE and LDPE having a Ml of 1.0, and at that time, a uniaxially stretched HDPE film of 30 p (draw ratio:: 6 times) was laminated upon the respective unstretched sheets to obtain laminates of 350 U (Examples 18 and 19). For comparison, sheets of 350 U having no uniaxially stretched film laminated were prepared (Comparative examples 7 and 8). The constitution and physical properties of these laminates and sheets are shown in Table 3. When the above
Examples are compared with Comparative examples corresponding thereto, it is apparent that the laminates of the Examples are superior to the sheets of the Comparative examples in heating behaviors, transparency and Young's modulus. Further, even when a stretched film of HDPE comprising a different resin is laminated onto a sheet of LDPE, as in Example 19, the effectiveness of the present invention is unchanged.
TABLE 3
Example Comparative
Unit example
18 19 7 8
Resin for laminate or HDPE LDPE HDPE LDPE
sheet
Raw Ml of resin for g/ material laminate or sheet 10mien. 1.0 1.0 1.0 1.0
Thickness of uniaxi
ally stretched film 11 30 30 30 30
of HDPE
Constitution Total thickness of of laminate laminate or sheet U 350 350 350 350
Thickness proportion
of film based on % 86 86
laminate
Haze % 68 36 95 60
Young's modulus Kg/mm2 69 28 65 22
Impact strength Kg-cm 30 < 30 < 30 < 30 <
Sagging quantity mm 18 20 21 23
Heating Recovered quantity % 100 100 95 98
behaviors Retention time sec. 35 32 32 27
Claims (5)
1. A laminate comprising a stretched thermoplastic resin film laminated to an unstretched thermoplastic
resin sheet, the stretched film forming 1 to 20% of the thickness of the laminate.
2. A laminate according to claim 1, wherein the unstretched sheet is of polyolefin resin.
3. A laminate according to claim 1 or 2, wherein the stretched film is of a polyolefin resin.
4. A laminate according to claim 3, wherein the stretched film was stretched at a draw ratio of 4 or more.
5. A process for producing thermoplastics articles by vacuum forming of a thermoplastic substrate,
wherein the substrate is a laminate according to any preceding claim.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP56176699A JPS5878749A (en) | 1981-11-04 | 1981-11-04 | Thermoplastic resin sheet for vacuum molding |
Publications (2)
Publication Number | Publication Date |
---|---|
GB2111908A true GB2111908A (en) | 1983-07-13 |
GB2111908B GB2111908B (en) | 1985-04-17 |
Family
ID=16018189
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB08231298A Expired GB2111908B (en) | 1981-11-04 | 1982-11-02 | Thermoplastic resin laminate for vacuum forming |
Country Status (3)
Country | Link |
---|---|
JP (1) | JPS5878749A (en) |
DE (1) | DE3240792C2 (en) |
GB (1) | GB2111908B (en) |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0245034A2 (en) * | 1986-05-02 | 1987-11-11 | Mitsui Petrochemical Industries, Ltd. | Packaging structure and process for production thereof |
US5318824A (en) * | 1986-05-02 | 1994-06-07 | Mitsui Petrochemical Industries, Ltd. | Packaging structure |
US5532325A (en) * | 1988-04-04 | 1996-07-02 | Chisso Corporation | Process for producing high stiffness polypropylene |
US6451446B1 (en) | 1998-05-21 | 2002-09-17 | Dow Global Technologies Inc. | Polypropylene/polystyrene multilayer film structures |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
FR2667015B1 (en) * | 1990-09-26 | 1995-09-15 | Cebal | METHOD FOR MANUFACTURING A HOLLOW CONTAINER FROM A MULTI-LAYERED STRIP OF PLASTIC MATERIAL AND CORRESPONDING CONTAINER. |
Family Cites Families (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE2160096A1 (en) * | 1971-12-03 | 1973-06-07 | 4 P Verpackungen Gmbh | Polyolefin laminated films - with good water-vapour and gas impermeability |
JPS5744464B2 (en) * | 1972-04-12 | 1982-09-21 | ||
JPS5439872B2 (en) * | 1972-05-15 | 1979-11-30 | ||
JPS4918976A (en) * | 1972-06-14 | 1974-02-19 | ||
JPS5334881A (en) * | 1976-09-13 | 1978-03-31 | Mitsubishi Plastics Ind Ltd | Multi-layer composite sheet for vacuum molding |
IT1075393B (en) * | 1977-04-13 | 1985-04-22 | Sir Soc Italiana Resine Spa | FLEXIBLE COUPLED FILMS FOR THE PACKAGING OF FOOD PRODUCTS |
DE2848736C2 (en) * | 1978-11-10 | 1986-12-18 | Sengewald, Karl-Heinz, Dr., 4802 Halle | Rigid, sterilizable, deep-drawn packaging |
-
1981
- 1981-11-04 JP JP56176699A patent/JPS5878749A/en active Granted
-
1982
- 1982-11-02 GB GB08231298A patent/GB2111908B/en not_active Expired
- 1982-11-04 DE DE3240792A patent/DE3240792C2/en not_active Expired
Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0245034A2 (en) * | 1986-05-02 | 1987-11-11 | Mitsui Petrochemical Industries, Ltd. | Packaging structure and process for production thereof |
EP0245034A3 (en) * | 1986-05-02 | 1988-09-28 | Mitsui Petrochemical Industries, Ltd. | Packaging structure and process for production thereof |
US4973375A (en) * | 1986-05-02 | 1990-11-27 | Mitsui Petrochemical Industries, Ltd. | Process for producing a composite sheet |
US5318824A (en) * | 1986-05-02 | 1994-06-07 | Mitsui Petrochemical Industries, Ltd. | Packaging structure |
US5532325A (en) * | 1988-04-04 | 1996-07-02 | Chisso Corporation | Process for producing high stiffness polypropylene |
US6451446B1 (en) | 1998-05-21 | 2002-09-17 | Dow Global Technologies Inc. | Polypropylene/polystyrene multilayer film structures |
Also Published As
Publication number | Publication date |
---|---|
DE3240792A1 (en) | 1983-05-11 |
GB2111908B (en) | 1985-04-17 |
JPS6141749B2 (en) | 1986-09-17 |
JPS5878749A (en) | 1983-05-12 |
DE3240792C2 (en) | 1986-09-04 |
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Legal Events
Date | Code | Title | Description |
---|---|---|---|
PCNP | Patent ceased through non-payment of renewal fee |