Polyethylene copolymers

Claim 2

A uniformly random, homogeneous copolymer of ethylene and an α, β-ethylenically unsaturated acid selected from the class consisting of acrylic acid and methacrylic acid, said copolymer exhibiting improved adhesion to solid metallic substrates and being composed of at least about 90% by weight ethylene and having at least 0.45% by weight of said unsaturated acid copolymerized therewith and uniformly randomly distributed along the copolymer chains, and said copolymer having a melt index of 0.01 to 30 g/10 min.

Claim 3

The copolymer of claim 1 in which the acid comonomer copolymerized with ethylene in the copolymer is acrylic acid.

Claim 4

The copolymer of claim 2 in which the melt index is 3.8 to 7.8 g/10 minutes and the acrylic acid content is 0.45 weight percent.

Claim 5

The copolymer of claim 2 in which the melt index is 4.0 to 5.3 g/10 minutes and the acrylic acid content is 2.5 weight percent.

Claim 6

The copolymer of claim 2 in which the melt index is 1.7 to 2.0 g/10 minutes and the acrylic acid content is 5.7 weight percent.

Claim 7

The copolymer of claim 1 in which the acid comonomer copolymerized with ethylene in the copolymer is methacrylic acid .

Claim 8

The copolymer of claim 6 in which the melt index is 1.3 to 2.5 g/10 minutes and the methacrylic acid content is 0.48 weight percent.

Claim 9

The copolymer of claim 6 in which the melt index is 4.4 to 5.2 g/10 minutes and the methacrylic acid content is 1.18 weight percent.

Claim 10

The copolymer of claim 6 in which the melt index is 2.9 to 3.6 g/10 minutes the methacrylic acid content is 2.29 weight percent.

Claim 11

The copolymer of claim 6 in which the melt index is 4.3 to 5.7 g/10 minutes and the methacrylic acid content is 5.21.

Claim 12

The copolymer of claim 10 in the form of a self-supporting film.

Claim 13

A laminated structure in which the binder is the copolymer of claim 10.

Claim 14

Metal foil coated with the copolymer of claim 1.

Claim 15

The coated metal foil of claim 13 in which the metal is aluminum.

Claim 16

Aluminum foil coated with the composition of claim 2.

Claim 17

Aluminum foil coated with the composition of claim 3.

Claim 18

Aluminum foil coated with the composition of claim 4.

Claim 19

Aluminum foil coated with the composition of claim 5.

Claim 20

Aluminum foil coated with the composition of claim 6.

Claim 21

Aluminum foil coated with the composition of claim 7.

Claim 22

Aluminum foil coated with the composition of claim 8.

Claim 23

Aluminum foil coated with the composition of claim 9.

Claim 24

Aluminum foil coated with the composition of claim 10.

Claim 25

A copolymer according to claim 2 in the form of a thin sheet consisting essentially thereof.

Claim 26

A copolymer according to claim 2 in the form of a layer in a consolidated laminar structure of at least two dissimilar laminar layers.

Claim 27

The process of preparing a uniformly random homogeneous copolymer of ethylene and an α,β-ethylenically unsaturated acid, selected from the class consisting of acrylic acid and methacrylic acid, said copolymer being composed of at least about 90% by weight ethylene, based on copolymer, and having at least 0.45% by weight of said unsaturated acid uniformly randomly distributed along the copolymer chains, by continuously charging ethylene, said unsaturated acid and a free radical initiator, selected from the group consisting of oxygen, peroxide and azo-bis compounds, into a single phase reaction zone stirred at a high rate and maintained at a preselected pressure of at least 1000 atmospheres of ethylene and at a preselected temperature maintained within narrow limits at a value between 90° and 280° C., the ratio of ethylene to unsaturated acid charged being in the range of 10,000/1 to 50/1 by weight, and maintaining a definite monomer to polymer ratio in the reaction zone and regulating the concentration of initiator fed into the reactor at a predetermined value while allowing said unsaturated acid and ethylene to copolymerize in said reaction zone, and continuously removing from reactor a stream consisting of unreacted ethylene, unreacted unsaturated acid, and the copolymer at a rate such that the reactor residence time permits conversion of 3 to 20% of the ethylene to polymer, through a pressure let-down valve to a zone maintained at substantially reduced pressure from which all reagents are flashed off leaving the copolymer product.

Claim 28

The process of preparing a uniformly random homogeneous copolymer of ethylene and an α,β-ethylenically unsaturated acid, selected from the class consisting of acrylic acid and methacrylic acid, said copolymer being composed of at least about 90% by weight ethylene, based on copolymer, and having at least 0.45% by weight of said unsaturated acid uniformly randomly distributed along the copolymer chains, by continuously charging ethylene, said unsaturated acid and a free radical initiator, selected from the group consisting of oxygen, peroxide and azo-bis compounds, into a single phase reaction zone stirred at a high rate and maintained at a preselected pressure of at least 1000 atmospheres of ethylene and at a preselected temperature maintained within narrow limits at a value between 90° and 280° C., the ratio of ethylene to unsaturated acid charged being in the range of 10,000/1 to 50/1 by weight, and maintaining a definite monomer to polymer ratio in the reaction zone and regulating the concentration of initiator fed into the reactor at a predetermined value while allowing said unsaturated acid and ethylene to copolymerize in said reaction zone, and continuously removing from reactor a stream consisting of unreacted ethylene, unreacted unsaturated acid, and the copolymer at a rate such that the reactor residence time permits conversion of 3 to 20% of the ethylene to polymer, through a pressure let-down valve to a zone maintained at substantially reduced pressure from which all reagents are flashed off leaving the copolymer product.

Claim 29

The process as set forth in claim 26 wherein the temperature is from 150° to 240° C. and the pressure from 1500 to 3000 atmospheres.

Claim 30

The process as set forth in claim 26 wherein the initiator is a peroxide.

Claim 31

The process as set forth in claim 26 wherein the polymerization is carried out in an inert solvent.

Claim 32

The process as set forth in claim 29 wherein the solvent is benzene.

Claim 33

The process of claim 26 wherein the acid comonomer is acrylic acid.