CA1124450A

CA1124450A - Polyethylene blend foams having improved compressive strength

Info

Publication number: CA1124450A
Application number: CA346,287A
Authority: CA
Inventors: Chung P. Park; Richard A. Bouton
Original assignee: Dow Chemical Co
Current assignee: Dow Chemical Co
Priority date: 1979-02-22
Filing date: 1980-02-22
Publication date: 1982-05-25
Also published as: DE3069050D1; AU5587580A; JPS55127440A; JPS5858368B2; EP0016348A2; AU530793B2; US4226946A; EP0016348B1; EP0016348A3

Abstract

Abstract of the Disclosure Low density foams from polyethylene blends having substantially closed cell structure and improved compressive strength are prepared using gel-forming extrusion technology. The polyethylene blend comprises from 35 to 60 weight percent of low density branched polyethylene in admixture with from 40 to 65 weight percent of intermediate density linear polyethylene.
An exemplary blowing agent is 1.2-dichlorotetra-fluoroethane, or 1,2-dichlorotetrafluoroethane used in an amount up to 0.12 gram-mole per 100 grams of resin blend.

Description

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POLYETHYLENE BLEND FOAMS HAVING
IMPROVED COMPRESSIVE STRENGTH

Polyethylene foams made from blends of low density polyethylene and intermediate density linear polyethylene. It particularly pertains to improvement in processes whereby are obtained foams having substan-tially closed-cell structure and improved compressive strength.

The term "compressive strength" as used herein means the property of foam articles as deter-mined by the test procedure described in ASTM D-3575-77, expressed in pounds per square inch (psi).

Low density closed-cell ethylenic polymer resin foams can be made by extrusion foaming of a normally solid thermoplastic ethylenic polymer resin such as low density branched polyethylene. The resin is heat-plastified and mixed under pressure with a volatile material such as 1,2-dichlorotetrafluoroethane to form a flowable gel which is then passed through a shaping orifice or die opening into a zone of lower pressure. The volatile component vaporizes, forming a gas phase cellular structure in the gel which cools to a solid cellular foam resin. Desirably, the gas cells are substantially uniform in size and distribution in 27,908-F -1-

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the foam body, and closed, i.e., separated from each other by membrane walls of resin. Although a number of general prlnciples are understood, much extrusion foaming technology is empirical. Prior attempts to make low density foam products from intermediate or high density linear polyethylenes have met numerous difficulties.

Polymer foams from blends of polyethylenes are known. In U.S. Patent 3,496,124 foams having high impact resistance are prepared from blends of 65 to 80 parts by weight low density polyethylene having densities from about 0.89 to 0.93 g/cc, with 35 to 20 parts by weight high density polyethylene having densities from about 0.94 to 0.97 g/cc. Japanese Patent Application No. 47-56,497 filed June 8, 1972, discloses a poly-ethylene foam prepared from a blend of polyethylenes of two different densities. More specifically, polyethylene resins of density <0.93 and density <0.94 are melt blended, pulverized, immersed in liquid blowing agents, and foamed at a temperature <20 higher than the arith-metical mean of the m.p. of the two polyethylenes.
U.S. Patent 3,793,239 discloses extrusion foaming of polymer blends of a crystalline polyolefin and 1 to 15 weight percent of a thermoplastic polymer using a two-component blowing agent. Blends of high density polyethylene and polypropylene are preferred.

U.S. Patent 3,351,569 teaches a method for making fine-celled polyolefin foam from crystalline polymers of ethylene or propylene using a liquid blowing agent and at least 10 percent by weight of a finely divided solid inorganic nucleating agent. Mixtures of two or more of crystalline polymers of ethylene or propylene can be used.

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Summarv of the Invention Foam resin products having improved compres-sive strength at a given foam density, and a substan-tially closed-cell structure are obtained by extrusion foaming of a polyethylene blend comprising from 35 to 60 weight percent of low density branched polyethylene having a density of about 0.910 to 0.930 in admixture with from 40 to 65 weight percent of intermediate density linear polyethylene having a density of about 0.931 to 0.940. The resulting polyethylene blend foams have densities from about 3.0 to 15.0 pounds per cubic foot (pcf) (0.048-0.240 g/cc) and preferably 3.0 to 7.0 pcf (0.048-0.112 g/cc). These foams have a sub-stantially closed-cell structure and average com-pressive strength at 10 percent deformation of about 7 to 170 psi (0.5 to 12.0 kg/cm2), preferably 7 to 60 psi (0.5 to 4.2 kg/cm2).

The term "average compressive strength" as used herein means an average of compressive strength values, expressed in psi or kg/cm2, in extrusion, vertical and transverse directions.

A particular benefit of this invention is the production of a low density foam from intermediate density linear polyethylene resin by blending therewith low density branched polyethylene.

The low density branched polyethylene may have a density from about 0.910 to 0.930 g/cc and a melt index from about 0.5 to 50 dg/min. and can be produced by the known high pressure polymerization processes.

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The intermediate density linear polyethylene may have a density from 0.931 to 0.940 and a melt index from 0.5 to 50 dg/min. Intermediate density linear polyethylene having these properties can be produced by Ziegler-type low pressure polymerization processes.

The starting polyethylene blend can also i contaln small portions of high density linear poly-ethylenes having a density greater than 0.940, provided that the resulting blend is extrudable.

The polyethylene blends of the present inven-tion can be prepared by admixing from 35 to 60 weight percent, preferably from 40 to 55 percent by weight, most preferably about 50 percent by weight, of a low density branched polyethylene and from 40 to 65 percent by weight, preferably from 45 to 60 percent by weight, most preferably about 50 percent by weight, of an intermediate density linear polyethylene. These poly-ethylenes can be blended together in a variety of different ways readily known in the art, and the manner of blending is not critical as long as the two poly-ethylenes are thoroughly mixed together.

Particularly useful blends of polyethylenes have a difference in melt index value of less than about 3.0 between the polyethylenes.

Blowing agents useful for making the poly-ethylene blend foams are well known: solids which decompose into gaseous products at the extrusion temperature and volatile liquids may be employed.
Particularly preferred are halogenated hydrocarbon compounds having from 1 to 4 carbon atoms. Examples of 27,908-F -4-' ;

such blowing agents are dichlorodifluoromethane, tri-chlorofluoromethane, chlorodifluoromethane, 1,2--dichlorotetrafluoroethane, l-chloro l,l-difluoroethane, l,l-dichlorotrifluoroethane, l,l-difluoroethane, 1-chloro-1,2,2,2-tetrafluoroethane, 1-chloro-1,1,2,2-tetrafluoroethane, 2,2-difluoropropane and 1,1,1-trifluoropropane. 1,2-dichlorotetrafluoroethane is most preferred. Cl 4 flurocarbons may also be used.
Although use of a single blowing agent is preferred, mixtures of two or more of such blowing agents may also be used.

The blowing agent is compounded into the j starting polyethylene blend in proportions to give the desired degree of expansion in the resulting foamed cellular product, usually up to about 20 volume expan-sion to make products having foamed densities down to about 0.048 g/cc (about 3.0 pcf). Depending on the starting proportion of blowing agent, the resulting foamed products have densities from about 3.0 to 15.0 pcf (0.048 to 0.240 g/cc), preferably from 3.0 to 7.0 pcf (0.048 to 0.112 g/cc).

The blowing agent is compounded into the polyethylene blend in conventional fashion to make a flowable gel, preferably in a mixing extruder using heat to palstify the resin blends, pressureto maintain the blowing agent in non-gaseous state, and mechanical working to obtain thorough mixing. The resulting gel is cooled, if necessary, and passed through a suitable die orifice into a zone of lower pressure, e.g., normal ambient air atmosphere, where it expands to a low density, cellular mass. As the foamed extrusion forms, it is withdrawn from the extruder, cooled and trans-ferred for further processing, storage or use.

27,908-F - 5 -,, ~,;

The resu;ting polyethylene blend foam is com-prised of substantially closed-cell structure and is flexible to bending and shaping. It has improved compressive strength measured at 10 percent deformation as compared to foam articles having eguivalent foam density but made from low density polyethylene alone.

The gas space in the cells of the polyethylene blend foam initially is filled with the volatile blowing agent(s) used to make the foam. As time passes, the blowing agent diffuses out of the foam and is gradually replaced by air diffusing into the foam cells. Ultimately, the foam gas space is essentially completely filled with air.

Finely divided solid materials such as calcium silicate, zinc stearate, magnesium silicate and the like can advantageously be incorporated with the polymer blend or gel prior to expansion to aid in controlling the size of the cells. They are usually employed in amounts up to one (1) percent by weight of the polymer.

Numerous fillers, pigments, lubricants, anti-oxidants and other known additives can also be incorpo-rated into the polyethylene blend and resulting foam.

The following specific working examples illustrate the invention. ~11 parts and percentages are by weight unless otherwise specified.

Exam~le 1 Polyethylene blend foams are made by con-tinuous extrusion from a conventional screw-type extruder with seguential zones usually designated feed zone, 27,908-F -6-_7_ ~ .a~

compression and melt zone, metering zone, and mixing zone. The extruder barrel is provided with conven-tional electric heaters for zoned temperature control and the usual instrumentation. An inlet openlng for fluid blowing agent under pressure and feed rate con-trol is provided in the extruder barrel between the metering zone and the mixing zone. The discharge end of the mixing zone of the extruder is connected through a cooler to a die orifice having generally rectangular configuration.

In practice, polyethylene resin granules are fed through the feed hopper to the extruder. The temperature in the metering zone is maintained in the range 180 i 20C. Blowing agent is pumped into the inlet between the metering and mixing zones at a pre-determined rate under pressure to maintain liquid phase. The mixed mass of molten polyethylene blend and blowing agent from the mixing zone is cooled in the temperature control zone to a substantially uniform temperature which is just above the temperature at which solid polymer would crystallize out of the gel.
For the polyethylene blends used in this example this is about 115C to 119C. Then it passes through the - die orifice. The mass emerging from the die orifice to atmospheric pressure expands and forms a cellular foam which is continuously withdrawn from the die as the foam forms. It cools and hardens to a strip of cellular, flexible, solid polyethylene blend foam.

In the tests described below the polyethylenes listed in Table I are used. Specific types and ratios of blends of these polyethylenes are listed in Table II. These blends are mixed in the feed hopper of the 27,908-F -7-extruder with magnesium silicate and calcium stearate as foam nucleation and cell size control agents at a ~ substantially constant rate as shown in Table II. The blowing agent, dichlorodifluoromethane (FC-12) or 1,2-dichlorotetrafluoroethane (FC-114), is also fed to the extruder at a substantially constant rate.

Various physical properties of the resulting extruded foam products are measured and recorded in Table II.

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--ll--From the data in Table II, it will be seen that polyethylene blend foams made in accordance with this invention have substantially improved compressive strength at 10 percent deformation as compared to the polyethylene foams of equivalent foam density made from low density polyethylene alone.

Measurement of percent open cell and a sub-jective evaluation of skin quality provide a good indication of the processibility of a polyethylene blend formulation. A low percentage of open cells is desirable as well as a smooth, uniform skin on the foam. Open cell concentrations of 15 to 30 percent indicate potential processibility problems and con-centrations greater than 30 percent are unacceptable.
Given this criteria, Test No 1.6 indicates that border line, yet still acceptable processibility is realized when the foam density is as low as 3.0 pcf. Attempts to lower the foam density below 3.0 pcf by using more blowing agent, as shown in Test No. 1.7, resulted in total collapse of the foam at the die. Test No 1.8 indicates that FC-12 may be substituted for FC-114 as the blowing agent.

Exam~le 2 Foams were produced from blends of various low density and linear polyethylenes listed in Table I
by continuous extrusion process of Example 1. Process-ibility characteristics of the foams listed in this Example are shown in Table III.

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27, 908-F -12-~13-From the results shown in Table IV, it will be seen, from Test Nos. 2.0 through 2.4, that the optimum polyethylene blends from the processibility standpoint comprises from 40 to 55 weight percent of low density polyethylene ln admixture wlth from 45 to 60 weight percent of intermediate density linear poly-ethylene. As shown in Test Nos. 2.3, 2.5, and 2.6 the best processibility is obtained by blendlng the linear polyethylene with a low density polyethylene of equiva-lent melt index, i.e., 5.0; the worst processibility is obtained from the blend of polyethylenes with the largest difference in melt indexes.

27,908-F -13-

Claims

THE EMBODIMENTS OF THE INVENTION IN WHICH AN EXCLUSIVE
PROPERTY OR PRIVILEGE IS CLAIMED AND DEFINED AS FOLLOWS:

1. In a method of making polymer resin foams by extrusion foaming wherein a normally solid thermo-plastic resin is heat-plastified, mixed with a blowing agent to form a flowable gel and then passed through a die opening into a zone of lower pressure to form a cellular resinous body, the improvement wherein the thermoplastic resin comprises a polyethylene blend comprising (1) 35 to 60 weight percent of low density branched polyethylene having a density from 0.910 to 0.930 in admixture with (2) 40 to 65 weight percent of intermediate density linear polyethylene having a density from 0.931 to 0.940 thereby producing poly-ethylene blend foams having density of about 3.0 to 15.0 pcf (0.048 to 0.240 g/cc), substantially closed--cell structure and compressive strength at 10 percent deformation of about 7 to 170 psi (0.5 to 12.0 kg/cm2).

2. The method of Claim 1 wherein the blend foams have density of 3.0 to 7.0 pcf (0.048 to 0.112 g/cc).

3. The method of Claim 2 wherein the blend foams have compressive strength at 10 percent deformation of 7 to 60 psi (0.5 to 4.2 kg/cm2).

4. The method of Claim 1 wherein the poly-ethylenes in the blend have a difference in melt index values of less than 3Ø

27,908-F -14-

5. A method of claim 1 wherein the blowing agent is a C1-4 fluorocarbon.

6. A method according to claim 1 wherein the blowing agent is 1,2-dichlorotetrafluoroethane or 1,1-dichloro-1,1-difluoromethane.

7. A polyethylene blend foam having substantially closed-cell structure, dimensional stability, and a compressive strength at 10 percent deformation of about 7 to 170 psi (0.5 to 12.0 kg/cm ), wherein the blend comprises (1) 35 to 60 weight percent of low density branched polyethylene having a density from 0.910 to 0.930 in admixture with (2) 40 to 65 weight percent of intermediate density linear polyethylene, having a density from 0.931 to 0.940 and the foam has a density of 3.0 to 15.0 pounds per cubic foot (0.048 to 0.240 g/cc).

8. The foam of claim 7 wherein the polyethylenes in the blend have a difference in melt index values of less than 3Ø

9. The foam of claim 7 when prepared by the process of claims 1-3.