US2014275302A1PendingUtilityA1
Polyethylene additive
Est. expiryMar 12, 2033(~6.7 yrs left)· nominal 20-yr term from priority
C08L 23/12C08K 5/56C08K 5/103C08L 23/06
59
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Claims
Abstract
A new additive for plastics (for example, polyethylene) is prepared by reacting a fatty acid ester of glycerol (such as glycerol monostearate) with a source of a reactive divalent metal selected from zinc, calcium, and magnesium. In an embodiment, Zinc oxide is the reactive divalent metal and the reaction is conducted in the presence of an acid such as zinc acetate. In one embodiment, a molar excess of zinc oxide (compared to the fatty acid ester) is used. The additive is suitable for use in the preparation of injection molded parts, rotomolded parts, and films.
Claims
exact text as granted — not AI-modifiedWhat is claimed is:
1 . A polyethylene additive prepared by the reaction of
a) a fatty acid ester of glycerol; with b) a divalent metal selected from zinc, calcium, and magnesium.
2 . The additive of claim 1 wherein the molar ratio of said fatty acid ester of glycerol to said divalent metal is from about 1/3 to about 3/1.
3 . The additive of claim 1 wherein said fatty acid ester of glycerol is glycerol monostearate or glycerol monooleate.
4 . The additive of claim 1 wherein said fatty acid ester of glycerol is glycerol monostearate.
5 . The additive of claim 1 wherein said divalent metal is zinc or magnesium.
6 . The additive of claim 1 wherein said divalent metal is zinc.
7 . The additive of claim 1 wherein said divalent metal is provided in the form of an oxide or hydroxide.
8 . The additive of claim 1 wherein said divalent metal is provided in the form of an oxide.
9 . The additive of claim 1 wherein said reaction is conducted in the presence of an acid catalyst.
10 . The additive of claim 1 wherein said reaction is conducted in the presence of zinc acetate and said divalent metal is provided in the form of zinc oxide.
11 . The additive of claim 1 wherein said reaction is conducted in the presence of magnesium acetate and said divalent metal is provided in the form of magnesium hydroxide.
12 . A process to prepare a polyethylene additive comprising reacting a fatty acid ester with a divalent metal.
13 . The process of claim 12 wherein said reaction occurs in the presence of an acid catalyst.
14 . The process of claim 13 wherein said fatty acid ester is glycerol monostearate, said divalent metal is zinc oxide and said acid catalyst is zinc acetate, wherein the molar ratio of said glycerol monostearate to said zinc oxide is from about 1/3 to about 3/1.
15 . The process of claim 13 wherein said fatty acid ester is glycerol monooleate, said divalent metal is magnesium hydroxide and said acid catalyst is magnesium acetate, wherein the molar ratio of said glycerol monooleate to said magnesium hydroxide is from about 1/3 to about 3/1.
16 . A polyethylene composition comprising
a) high density polyethylene; and b) from about 500 to about 5000 parts per million by weight of the additive of claim 1 .
17 . The polyethylene composition of claim 16 wherein said high density polyethylene has a melt index of from about 0.5 to about 10 grams per 10 minutes and a density of from about 0.955 to about 0.970 g/cc; wherein melt index is determined by ASTM D-1238 at 190° C. and density is determined by ASTM D-1505.
18 . A polyethylene composition comprising
a) a first high density polyethylene having a density of from about 0.95 to about 0.97 g/cc; b) a second high density polyethylene having a density of from about 0.955 to about 0.965 g/cc; and c) from about 500 to about 5000 parts per million by weight of the additive of claim 1 ;
wherein said first high density polyethylene has an I 2 value at least 10 times greater than the I 2 ′ value of said second high density polyethylene, and the I 2 ′ value of said second high density polyethylene is from about 0.1 to about 2 grams/10 minutes; wherein melt index is determined by ASTM D-1238 at 190° C. and density is determined by ASTM D-1505.
19 . The polyethylene composition of claim 18 wherein the first high density polyethylene is SCLAIR® 79F and the second high density polyethylene is selected from SCLAIR® 19G, MARFLEX® 9659 and ALATHON® L 5885.
20 . A blown film prepared from the composition of claim 16 , characterized in that said blown film has at least about 20% improvement in WVTR compared to a film made without said additive.Cited by (0)
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