CA1072700A - Resin formulation for rotational molding and shaped structures - Google Patents
Resin formulation for rotational molding and shaped structuresInfo
- Publication number
- CA1072700A CA1072700A CA274,491A CA274491A CA1072700A CA 1072700 A CA1072700 A CA 1072700A CA 274491 A CA274491 A CA 274491A CA 1072700 A CA1072700 A CA 1072700A
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- ethylene
- component
- propylene
- blend
- vinyl acetate
- Prior art date
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Abstract
Abstract of the Disclosure A three component blend of polymers comprising a polyethylene homopolymer or ethylene-alkene copolymer with an ethylene-vinyl acetate copolymer and either an ethylene-propylene copolymer or an ethylene-propylene-diene terpolymer. These three component blends are particularly suitable for rotational molding of shaped structures as they have synergistic properties of environmental stress crack resistance and high impact strength of the finished products. The disclosure also includes shaped structures comprising these blends.
Description
1~727~
RESIN FORMULATION FOR ROTATIONAL
MOLDING AND SHAPED STRUCTURES
Background of the Invention : . This invention relates to three component blends of high density polyethylene with specified copolymers and combin-ations of copolymers that are particularly useEul for rotational molding and relates also to the structures produced therefrom. ~ :
U. S. patent 3,261,889 discloses a blend of a low . density polyethylene and an ethylene-propylene-diene terpolymer to improve environmental stress crack resistance (ESCR)~ (A
table of abbreviations is presented at the end of this specifi-cation.~ The three component blends of this invention have the ESCR improvement significantly above that achieved via a two component blend due to the unexpected syneryism of the blend components.
,~
- 1- ~ :
~L~72700 In the conventional rotational molding resins and blends it is customary to use polyethylene of narrow molecular weight distribution and with low melt f:Low to achieve high impact strength. These prior resins are difficult to process apparently due to their high apparent melt viscosity. They are generally not warp resistant. It has been known to blend EVA (ethylene-vinyl acetate copo~Lymer) with polyethylene in order to improve the impact strength of the resin. However, polyethylene-EVA copolymer blends are not nearly as effective as the blends of this invention in improved impact resistance of rotomolded structures. In addition, these prior and con-ventional rotational molding blends containing polyethylene do not have the above advantages of the blends of this inven-tion.
, !
Summary of the Invention . , _ , -- . , The blends of this invention can be generally summarize~
as comprising (1) either a high density polyethylene or an ethylene-alkene copolymer containing 4 or 6 carbon atoms in the alkene group blended with (2) either an ethylene-propylene ; 20 essentially random copolymer or an essentially random terpolymer of ethylene and propylene and ~ monomer that is either 1,4-hexadiene, 5-ethylidine-2-norbornene and 5-methylene-2-norbor-nene, and (3) ethylene-vinyl acetate copolymer.
Preferred ranges of amounts are 60~80 wt.% of the poly-ethylene or ethylene-alkene copolymer with 5-20 wt.% of ethylene-propylene copolymer or terpolymer and 5-30 wt.% of EVA for a total of 100~. In the ethylene-propylene copolymers the preferred proportions are 40-95 wt.% of ethylene and 5-50 wt.% of propylene for a total of 100~. In the terpolymer there ;`
is preferably 40-95 wt.% of ethylene, -5-60 wt.% of propylene and 1-8 wt.% of the third monomer listed above so that the total is 10~%.
." ., 3L~7270~
., The ethylene-vinyl acetate copolymers preEerably con-tain 65-95 wt.% of ethylene and 5-35 wt.% of vinyl acetate for a total of 100~.
, Description of the Preferred Emhodiments The blends of this invention have characteristics that make them highly useful for rotational molding to produce molded shaped structures. Thus the blends of this invention ~-have good processability, high impact strength, produce smooth surfaces in the rotationally molded structures with a virtual absence of warpage in the structures, have easy flow during the rotational molding and the structures produced have a high resistance to environmental stress cracking.
To obtain maximum improvement in the impact strength and ESCR of the blend, the preferred elastomer component, i.e.
ethylene-propylene copoiymer and ethylene-propylene-diene ter-polymer, should have a narrow molecular weight distribution as ;~
measured on the Gel Permeation Chromatograph. Tests have shown that the blend properties improve with narrowing molecular weight distribution of the elastomer component of this invention and 20 with incre~asing elastomer content up to the concentration dis- -closed herein.
The blends of this invention may be prepared with any : , desired mixer or blender so long as the resulting blends are homogeneous and thlerefore uniform. Thus the mixers may be either roll mills, banburies, kneaaers or extruders or the like and the mixing temperatures are preferably above the softening point of the ingredients and, for example, may be within the range of 175-500~F. The blends of this invention are processed in the normal manner in the thermoplastic range of ~e particular blend to produce 30 shaped structures that are themselves homogeneous and that have desired improved characteristics including those speci~ically noted above.
~C3727()~
Certain values which are important for the proper pro-cessing of the blends of this invention are standard procedures that are customarily used in this art. Thus the test for en-vironmental stress cracking of ethylene containing plastics is the test designated D1693-70 of A.S.T.M. The test for impact resistance of plastics is designated as ASTM Method A of D256-56.
The standard method used for testing tensile-impact energy to ~;
break plastics is desginated as ASTM D 1822-68 with the actual test specimen being that shown in Figure 4B of the paper entitled "Test for Tensile-Impact Energy to Break Plastics" at page 590.
Mooney viscosity data is obtained according to ASTM-D1646, Viscosity And Curing Characteri~ics o~ Rubber By The Shearing Disc Viscometer.
The high density polyethylene used in this invention includes ethylene homopolymers as well as ethylene butene-l and ethylene hexene-l copolymers preferably with an annealed density ~ange of 0.940 to 0.970. These high density polyethylene resins can be produced by Ziegler or modified Zieglex catalysts, chromium oxide catalysts, molybdenum oxide catalysts or any of the available processes for producing essentially linear crystalline polyethylene.
The EVA copolymers used in this invention can be p~oduced by free ~ r radical catalysts at high pressures. The vinyl ace-tate content in these copolymers can range from 5% to 35%. The ethylene-propylene~
copolymers and ethylene-propylene-diene terpolymers used in this invention are essential~y random copolymers that can be produced via the transition metal catalyst. The preferred compound should -have an ethylene content above 40% with high molecular weight and ` narrow molecular weight distribution. ~here an ethylene-alkene (alkene = 4 or 6 carbons) copolymer is used in the blend the alkene content may be up to lO~t.% of the ethylene-alkene copolymer with 30 the ethylene being from 90-100 wt.%.
The three component blends of this invention produce a synergistic effect with relation to the impact strength and ESCR
1~7;~70(~
properties of the resin in that the overall effect is greater than that which would be expected by t~e add~ive properties of the individual components.
The preferred ethylene-vinyl acetate copolymer should contain at least 5% vinyl acetate with an MI of 1 or above. The blend properties are shown to improvle with increasing vinyl acetate concentration up to the including the preferred range disclosed herein. The processability of the blend on rotational molding machines improves when the polyethylene and the EVA copolymer components have a good match of melt viscositie5.
Specific Examples Example 1 A two component blend of 15% ethylene-propylene-diene terpolymer having a Mooney viscosity of about 50 (ML1~4/250F~) and 85% of ethylene-hexene-l copolymer of 0.955 density and 18 MI
was produced on a Banbury mixer. The mixing time was 3--1/2 minutes, achieving a drop temperature of approximately 320~F. The mixture was dropped into an extruder and pelletized. The resulting blend has a nominal MI of 6.5 and 0.942 density. A comparison of parts rotomolded from this blend and other commercial rotomolding resins under the same molding conditions show that the blend of this example is characterized ~y excellent impact strength and dimen-sional stability (very low warpage) plus smooth glass-like inter~or surfaces and an unusually wide range of molding temperature and cycle times.
A comparison between the physical properties of roto-molded parts from ~he blend in Example 1 and a direct synthesis copolymer rotomolding resin is shown in Chart I.
.
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CHART I
Physical Properties of ~otomolded Parts Blend in HDPE Copolymer _ Ex. 1 ~otomoldi~g Resin MI (g/10 min) 7.1 4.5 ; Density (g/cc) 0.936 0.935 Tensile Impact (ft-lbs/in2) 64 21 Notched ~zod (ft-lbs/in width) 4.6(P) 0.81(C) ~ell ESCR F50 (hrs~ 4.3 break on bending The above results indicate that the blend of this invention has significantly better properties on rotomolded structures than that of HDPE copolymer res;ns with similar MI and density prop-erties but produced by direct synthesis.
Example 2 .
A thxee component blend of lOg ethylene-propylene-diene terpolymer with 20~ 0.950 density, 2.5 MI~ 27.6% vinyl acetate content EVA copolymer plus 70~ of a 0.964 density, 12 MI homo-polymer polye~hylene was produced on a Banbury mixer and pelletizedas in Example 1. Rotomolded parts from this nominal 5.5 MI, 0.~53 density blend were characterized by excellent impact resistance and superior ESCR (about 60 hours). The impact strength and especially the ESCR are the result of a synergistic effect between the EPDM and the EVA copolymer. Chart II shows this effect for compression molded samples.
Example 3 A blend of 30% EPDM and 70~ homopolymer is prepared using the same materials and procedures as in Example 2. Physical ; 30 properties of cOmpressiQn molded plaques are shown in Chart II.
Example 4 A blend of 30% EVA copolymer and 70% homopolymer poly-ethylene is prepared using the same materials and procedures as 1~7;~76)0 in Example 2. Physical properties of compression molded plaques are shown in Chart II hereinafter.
Examples 5-12 The effect of EPDM and EVA concentration on the physical properties of compression molded plaques from the resulting blends is shown in Chart II~ hereinafter. The materials and mixing con-ditions are the same as in Example 2 except that the hexene co-polymer used in Exa~ple 1 was used in place of the homopolymer used in Exampla 2. This data also shows in Example 12 the synergistic ` 10 effect of the PE-EVA-EPDM combination.
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The following Examples 13-32 of Chart IV illustrate the synergistic results in environmental stress crack resistance achieved with the three component blends of this invention whexe the relatively expensive Component (2) is used in the relatively small pro~ortions of 5-20 weight percent.
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All parts and percentages herein are by weight.
Abbreviations C ~ complete break p - partial break - N o B . - no break ' EPDM - ethylene-propylene-diene terpolymer `. EPR - ethylene-prop~lene copolymer rubber ~ ESCR - environmental stress crack resistance : EVA - ethylene-vinyl acetate copolymer :
:;~ 10 HDPE - high density polyethylene MI - melt index MWD - molecular weight distribution . - Having described our invention as related to the em-boaiments set out herein) it is our intention that the invention be not limited by any of the details of description, unless otherwise specified, but rather be construed broadly within its .
spirit and scope as set out in the appended claims.
:
,;
~" ;.
~.
,
RESIN FORMULATION FOR ROTATIONAL
MOLDING AND SHAPED STRUCTURES
Background of the Invention : . This invention relates to three component blends of high density polyethylene with specified copolymers and combin-ations of copolymers that are particularly useEul for rotational molding and relates also to the structures produced therefrom. ~ :
U. S. patent 3,261,889 discloses a blend of a low . density polyethylene and an ethylene-propylene-diene terpolymer to improve environmental stress crack resistance (ESCR)~ (A
table of abbreviations is presented at the end of this specifi-cation.~ The three component blends of this invention have the ESCR improvement significantly above that achieved via a two component blend due to the unexpected syneryism of the blend components.
,~
- 1- ~ :
~L~72700 In the conventional rotational molding resins and blends it is customary to use polyethylene of narrow molecular weight distribution and with low melt f:Low to achieve high impact strength. These prior resins are difficult to process apparently due to their high apparent melt viscosity. They are generally not warp resistant. It has been known to blend EVA (ethylene-vinyl acetate copo~Lymer) with polyethylene in order to improve the impact strength of the resin. However, polyethylene-EVA copolymer blends are not nearly as effective as the blends of this invention in improved impact resistance of rotomolded structures. In addition, these prior and con-ventional rotational molding blends containing polyethylene do not have the above advantages of the blends of this inven-tion.
, !
Summary of the Invention . , _ , -- . , The blends of this invention can be generally summarize~
as comprising (1) either a high density polyethylene or an ethylene-alkene copolymer containing 4 or 6 carbon atoms in the alkene group blended with (2) either an ethylene-propylene ; 20 essentially random copolymer or an essentially random terpolymer of ethylene and propylene and ~ monomer that is either 1,4-hexadiene, 5-ethylidine-2-norbornene and 5-methylene-2-norbor-nene, and (3) ethylene-vinyl acetate copolymer.
Preferred ranges of amounts are 60~80 wt.% of the poly-ethylene or ethylene-alkene copolymer with 5-20 wt.% of ethylene-propylene copolymer or terpolymer and 5-30 wt.% of EVA for a total of 100~. In the ethylene-propylene copolymers the preferred proportions are 40-95 wt.% of ethylene and 5-50 wt.% of propylene for a total of 100~. In the terpolymer there ;`
is preferably 40-95 wt.% of ethylene, -5-60 wt.% of propylene and 1-8 wt.% of the third monomer listed above so that the total is 10~%.
." ., 3L~7270~
., The ethylene-vinyl acetate copolymers preEerably con-tain 65-95 wt.% of ethylene and 5-35 wt.% of vinyl acetate for a total of 100~.
, Description of the Preferred Emhodiments The blends of this invention have characteristics that make them highly useful for rotational molding to produce molded shaped structures. Thus the blends of this invention ~-have good processability, high impact strength, produce smooth surfaces in the rotationally molded structures with a virtual absence of warpage in the structures, have easy flow during the rotational molding and the structures produced have a high resistance to environmental stress cracking.
To obtain maximum improvement in the impact strength and ESCR of the blend, the preferred elastomer component, i.e.
ethylene-propylene copoiymer and ethylene-propylene-diene ter-polymer, should have a narrow molecular weight distribution as ;~
measured on the Gel Permeation Chromatograph. Tests have shown that the blend properties improve with narrowing molecular weight distribution of the elastomer component of this invention and 20 with incre~asing elastomer content up to the concentration dis- -closed herein.
The blends of this invention may be prepared with any : , desired mixer or blender so long as the resulting blends are homogeneous and thlerefore uniform. Thus the mixers may be either roll mills, banburies, kneaaers or extruders or the like and the mixing temperatures are preferably above the softening point of the ingredients and, for example, may be within the range of 175-500~F. The blends of this invention are processed in the normal manner in the thermoplastic range of ~e particular blend to produce 30 shaped structures that are themselves homogeneous and that have desired improved characteristics including those speci~ically noted above.
~C3727()~
Certain values which are important for the proper pro-cessing of the blends of this invention are standard procedures that are customarily used in this art. Thus the test for en-vironmental stress cracking of ethylene containing plastics is the test designated D1693-70 of A.S.T.M. The test for impact resistance of plastics is designated as ASTM Method A of D256-56.
The standard method used for testing tensile-impact energy to ~;
break plastics is desginated as ASTM D 1822-68 with the actual test specimen being that shown in Figure 4B of the paper entitled "Test for Tensile-Impact Energy to Break Plastics" at page 590.
Mooney viscosity data is obtained according to ASTM-D1646, Viscosity And Curing Characteri~ics o~ Rubber By The Shearing Disc Viscometer.
The high density polyethylene used in this invention includes ethylene homopolymers as well as ethylene butene-l and ethylene hexene-l copolymers preferably with an annealed density ~ange of 0.940 to 0.970. These high density polyethylene resins can be produced by Ziegler or modified Zieglex catalysts, chromium oxide catalysts, molybdenum oxide catalysts or any of the available processes for producing essentially linear crystalline polyethylene.
The EVA copolymers used in this invention can be p~oduced by free ~ r radical catalysts at high pressures. The vinyl ace-tate content in these copolymers can range from 5% to 35%. The ethylene-propylene~
copolymers and ethylene-propylene-diene terpolymers used in this invention are essential~y random copolymers that can be produced via the transition metal catalyst. The preferred compound should -have an ethylene content above 40% with high molecular weight and ` narrow molecular weight distribution. ~here an ethylene-alkene (alkene = 4 or 6 carbons) copolymer is used in the blend the alkene content may be up to lO~t.% of the ethylene-alkene copolymer with 30 the ethylene being from 90-100 wt.%.
The three component blends of this invention produce a synergistic effect with relation to the impact strength and ESCR
1~7;~70(~
properties of the resin in that the overall effect is greater than that which would be expected by t~e add~ive properties of the individual components.
The preferred ethylene-vinyl acetate copolymer should contain at least 5% vinyl acetate with an MI of 1 or above. The blend properties are shown to improvle with increasing vinyl acetate concentration up to the including the preferred range disclosed herein. The processability of the blend on rotational molding machines improves when the polyethylene and the EVA copolymer components have a good match of melt viscositie5.
Specific Examples Example 1 A two component blend of 15% ethylene-propylene-diene terpolymer having a Mooney viscosity of about 50 (ML1~4/250F~) and 85% of ethylene-hexene-l copolymer of 0.955 density and 18 MI
was produced on a Banbury mixer. The mixing time was 3--1/2 minutes, achieving a drop temperature of approximately 320~F. The mixture was dropped into an extruder and pelletized. The resulting blend has a nominal MI of 6.5 and 0.942 density. A comparison of parts rotomolded from this blend and other commercial rotomolding resins under the same molding conditions show that the blend of this example is characterized ~y excellent impact strength and dimen-sional stability (very low warpage) plus smooth glass-like inter~or surfaces and an unusually wide range of molding temperature and cycle times.
A comparison between the physical properties of roto-molded parts from ~he blend in Example 1 and a direct synthesis copolymer rotomolding resin is shown in Chart I.
.
. .
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CHART I
Physical Properties of ~otomolded Parts Blend in HDPE Copolymer _ Ex. 1 ~otomoldi~g Resin MI (g/10 min) 7.1 4.5 ; Density (g/cc) 0.936 0.935 Tensile Impact (ft-lbs/in2) 64 21 Notched ~zod (ft-lbs/in width) 4.6(P) 0.81(C) ~ell ESCR F50 (hrs~ 4.3 break on bending The above results indicate that the blend of this invention has significantly better properties on rotomolded structures than that of HDPE copolymer res;ns with similar MI and density prop-erties but produced by direct synthesis.
Example 2 .
A thxee component blend of lOg ethylene-propylene-diene terpolymer with 20~ 0.950 density, 2.5 MI~ 27.6% vinyl acetate content EVA copolymer plus 70~ of a 0.964 density, 12 MI homo-polymer polye~hylene was produced on a Banbury mixer and pelletizedas in Example 1. Rotomolded parts from this nominal 5.5 MI, 0.~53 density blend were characterized by excellent impact resistance and superior ESCR (about 60 hours). The impact strength and especially the ESCR are the result of a synergistic effect between the EPDM and the EVA copolymer. Chart II shows this effect for compression molded samples.
Example 3 A blend of 30% EPDM and 70~ homopolymer is prepared using the same materials and procedures as in Example 2. Physical ; 30 properties of cOmpressiQn molded plaques are shown in Chart II.
Example 4 A blend of 30% EVA copolymer and 70% homopolymer poly-ethylene is prepared using the same materials and procedures as 1~7;~76)0 in Example 2. Physical properties of compression molded plaques are shown in Chart II hereinafter.
Examples 5-12 The effect of EPDM and EVA concentration on the physical properties of compression molded plaques from the resulting blends is shown in Chart II~ hereinafter. The materials and mixing con-ditions are the same as in Example 2 except that the hexene co-polymer used in Exa~ple 1 was used in place of the homopolymer used in Exampla 2. This data also shows in Example 12 the synergistic ` 10 effect of the PE-EVA-EPDM combination.
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The following Examples 13-32 of Chart IV illustrate the synergistic results in environmental stress crack resistance achieved with the three component blends of this invention whexe the relatively expensive Component (2) is used in the relatively small pro~ortions of 5-20 weight percent.
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All parts and percentages herein are by weight.
Abbreviations C ~ complete break p - partial break - N o B . - no break ' EPDM - ethylene-propylene-diene terpolymer `. EPR - ethylene-prop~lene copolymer rubber ~ ESCR - environmental stress crack resistance : EVA - ethylene-vinyl acetate copolymer :
:;~ 10 HDPE - high density polyethylene MI - melt index MWD - molecular weight distribution . - Having described our invention as related to the em-boaiments set out herein) it is our intention that the invention be not limited by any of the details of description, unless otherwise specified, but rather be construed broadly within its .
spirit and scope as set out in the appended claims.
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Claims (10)
1. A blend of polymers especially suitable for the rotational molding of shaped structures, comprising: a three component blend of (1) 60-80 wt.% of a member of a first class consisting of high density polyethylene and high density ethylene-alkene copolymers containing 4 or 6 carbon atoms in the alkene group with (2) 5-20 wt.% of a member of a second class consisting of ethylene-propylene essentially random co-polymer and an essentially random terpolymer of ethylene-propylene monomer in which the monomer is selected from the group consisting of 1,4-hexadiene, 5-ethylidine-2-norbornene and 5-methylene-2-norbornene, and (3) 5-30 wt.% of a copolymer of ethylene-vinyl acetate for a total of 100%.
2. The blend of claim 1 wherein said component (2) consists essentially of a said ethylene-propylene copolymer con-taining 40-95 wt.% of ethylene and 5-60 wt.% of propylene for a total of 100%, and said component (3) contains 65-95 wt.% of ethylene and 5-35 wt.% of vinyl acetate for a total of 100%.
3. The blend of claim 1 wherein component (2) consists essentially of a said terpolymer containing 40-95 wt.% of ethylene, 5-60 wt.% of propylene and 1-8 wt.% of said group monomer for a total of 100%, and said ethylene-vinyl acetate copolymer contains 65-95 wt.% of ethylene and 5-35 wt.% of vinyl acetate for a total of 100%.
4. A blend of polymers especially suitable for rota-tional molding of shaped structures, comprising: a three component blend of 70 wt.% of high density polyethylene as a first component, 10 wt.% of ethylene-propylene essentially random copolymer as a second component and 20 wt.% of ethylene-vinyl acetate as a third component.
5. A blend of polymers especially suitable for rota-tional molding of shaped structures, comprising: a three component blend of 70 wt.% of high density polyethylene as a first component, 10 wt.% of ethylene-propylene-monomer essentially random terpolymer as a second component and 20 wt.% of ethylene-vinyl acetate as a third component.
6. A rotationally molded shaped structure, comprising:
a three component blend of (1) 60-80 wt.% of a member of a first class consisting of high density polyethylene and high density ethylene-alkene copolymers containing 4 or 6 carbon atoms in the alkene group with (2) 5-20 wt.% of a member of a second class consisting of ethylene-propylene essentially random copolymer and an essentially random terpolymer of ethylene-propylene-monomer in which the monomer is selected from the group consisting of 1,4-hexadiene, 5-ethylidine-2-norbornene and 5-methylene-2-nor-bornene, and (3) 5-30 wt.% of a copolymer of ethylene-vinyl acetate for a total of 100%.
a three component blend of (1) 60-80 wt.% of a member of a first class consisting of high density polyethylene and high density ethylene-alkene copolymers containing 4 or 6 carbon atoms in the alkene group with (2) 5-20 wt.% of a member of a second class consisting of ethylene-propylene essentially random copolymer and an essentially random terpolymer of ethylene-propylene-monomer in which the monomer is selected from the group consisting of 1,4-hexadiene, 5-ethylidine-2-norbornene and 5-methylene-2-nor-bornene, and (3) 5-30 wt.% of a copolymer of ethylene-vinyl acetate for a total of 100%.
7. The structure of claim 6 wherein said component (1) consists essentially of a said ethylene-propylene copolymer containing 40-95 wt.% of ethylene and 5-60 wt.% of propylene for a total of 100%, and said component (3) contains 65-95 wt.%
of ethylene and 5-35 wt.% of vinyl acetate for a total of 100%.
of ethylene and 5-35 wt.% of vinyl acetate for a total of 100%.
8. The structure of claim 6 wherein said component (2) consists essentially of a said terpolymer containing 40-95 wt.% of ethylene, 5-60 wt.% of propylene and 1-8 wt.% of said group monomer for a total of 100%, and said ethylene-vinyl acetate copolymer contains 65-95 wt.% of ethylene and 5-35 wt.% of vinyl acetate for a total of 100%.
9. A rotationally molded shaped structure, comprising:
a three component blend of 70 wt.% of high density polyethylene as a first component, 10 wt.% of ethylene-propylene essentially random copolymer as a second component and 20 wt.% of ethylene-vinyl acetate as a third component.
a three component blend of 70 wt.% of high density polyethylene as a first component, 10 wt.% of ethylene-propylene essentially random copolymer as a second component and 20 wt.% of ethylene-vinyl acetate as a third component.
10. A rotationally molded shaped structure, comprising:
a three component blend of 70 wt.% of high density polyethylene as a first component, 10 wt.% of ethylene-propylene-monomer essentially random terpolymer as a second component and 20 wt.%
of ethylene-vinyl acetate as a third component.
a three component blend of 70 wt.% of high density polyethylene as a first component, 10 wt.% of ethylene-propylene-monomer essentially random terpolymer as a second component and 20 wt.%
of ethylene-vinyl acetate as a third component.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CA274,491A CA1072700A (en) | 1977-03-22 | 1977-03-22 | Resin formulation for rotational molding and shaped structures |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CA274,491A CA1072700A (en) | 1977-03-22 | 1977-03-22 | Resin formulation for rotational molding and shaped structures |
Publications (1)
Publication Number | Publication Date |
---|---|
CA1072700A true CA1072700A (en) | 1980-02-26 |
Family
ID=4108214
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CA274,491A Expired CA1072700A (en) | 1977-03-22 | 1977-03-22 | Resin formulation for rotational molding and shaped structures |
Country Status (1)
Country | Link |
---|---|
CA (1) | CA1072700A (en) |
-
1977
- 1977-03-22 CA CA274,491A patent/CA1072700A/en not_active Expired
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