Use of polyglycerol aliphatic ether emulsifiers in making high internal phase emulsions that can be polymerized to provide absorbent foams

Claim 2

A process for the preparation of an high internal phase emulsion, which comprises the step of forming a water-in-oil emulsion from: A) an oil phase comprising: 1) from about 65 to about 98% by weight of a monomer component capable of forming a polymer having a Tg of about 35° C. or lower and comprising: a) from about 30 to about 85% by weight of at least one substantially water-insoluble monofunctional monomer capable of forming an atactic amorphous polymer having a Tg of about 25° C. or lower; b) from 0 to about 40% by weight of at least one substantially water-insoluble monofunctional comonomer; and c) from about 5 to about 40% by weight of at least one substantially water-insoluble, polyfunctional crosslinking agent; and 2) from about 2 to about 35% by weight of an emulsifier component which is soluble in the oil phase and which is suitable for forming a stable water-in-oil emulsion, said emulsifier component comprising at least about 40% linear diglycerol monoaliphatic ethers and at least about 60% polyglycerol aliphatic ethers having C 10 -C 24 aliphatic groups; and B) a water phase comprising an aqueous solution containing: 1) from about 0.2 to about 20% by weight of a water-soluble electrolyte; and 2) an effective amount of a polymerization initiator; C) a volume to weight ratio of the water phase to the oil phase in the range of from about 12:1 to about 125:1.

Claim 3

The process of claim 1 wherein the ratio of the water phase to the oil phase is in the range of from about 20:1 to about 90:1.

Claim 4

The process of claim 2 wherein the ratio of the water phase to the oil phase is in the range of from about 25:1 to about 75:1.

Claim 5

The process of claim 2 wherein the oil phase comprises from about 80 to about 97% by weight monomer component and from about 3 to about 20% by weight emulsifier component.

Claim 6

The process of claim 4 wherein the oil phase comprises from about 90 to about 97% by weight monomer component and from about 3 to about 10% by weight emulsifier component.

Claim 7

The process of claim 4 wherein the monomer component comprises: a) from about 50 to about 70% by weight of a monomer selected from the group consisting of butyl acrylate, hexyl acrylate, octyl acrylate, 2-ethylhexyl acrylate, nonyl acrylate, decyl acrylate, dodecyl acrylate, isodecyl acrylate, tetradecyl acrylate, benzyl acrylate, nonylphenyl acrylate, hexyl methacrylate, octyl methacrylate, nonyl methacrylate, decyl methacrylate, isodecyl methacrylate, dodecyl methacrylate, tetradecyl methacrylate, N-octadecyl acrylamide, p-n-octylstyrene, isoprene, 1,3-butadiene, 1,3-hexadiene, 1,3-heptadiene, 1,3-octadiene, 1,3-nonadiene, 1,3-decadiene, 1,3-undecadiene, 1,3-dodecadiene, 2-methyl-1,3-hexadiene, 6-methyl-1,3-heptadiene, 7-methyl-1,3-octadiene, 1,3,7-octatriene, 1,3,9-decatriene, 1,3,6-octatriene, 2,3-dimethyl-1,3-butadiene, 2-amyl-1,3-butadiene, 2-methyl-1,3-pentadiene, 2,3-dimethyl-1,3-pentadiene, 2-methyl-3-ethyl-1,3-pentadiene, 2-methyl-3-propyl-1,3-pentadiene, 2,6-dimethyl-1,3,7-octatriene, 2,7-dimethyl-1,3,7-octatriene, 2,6-dimethyl-1,3,6-octatriene, 2,7-dimethyl-1,3,6-octatriene, 7-methyl-3-methylene-1,6-octadiene, 2,6-dimethyl-1,5,7-octatriene, 1-methyl-2-vinyl-4,6-hepta-dieny-3,8-nonadienoate, 5-methyl-1,3,6-heptatriene, 2-ethylbutadiene, and mixtures thereof; b) from about 5 to about 40% by weight of a comonomer selected from the group consisting of styrene, ethyl styrene, methyl methacrylate, and mixtures thereof; and c) from about 10 to about 30% by weight of a crosslinking agent selected from the group consisting of divinylbenzenes, divinyltoluenes, divinylxylenes, divinylnaphthalenes divinylalkylbenzenes, divinylphenanthrenes, trivinylbenzenes, divinylbiphenyls, divinyldiphenylmethanes, divinylbenzyls, divinylphenylethers, divinyldiphenylsulfides, divinylfurans, divinylsulfone, divinylsulfide, divinyldimethylsilane, 1,1'-divinylferrocene, 2-vinylbutadiene, ethylene glycol dimethacrylate, neopentyl glycol dimethacrylate, 1,3-butanediol dimethacrylate, diethylene glycol dimethacrylate, hydroquinone dimethacrylate, catechol dimethacrylate, resorcinol dimethacrylate, triethylene glycol dimethacrylate, polyethylene glycol dimethacrylate, trimethylolpropane trimethacrylate, pentaerythritol tetramethacrylate, 1,4-butanediol dimethacrylate, 1,6-hexanediol diacrylate, 1,4-butanediol diacrylate, tetramethylene diacrylate, trimethyolpropane triacrylate, pentaerythritol tetraacrylate, N-methylolacrylamide, N-methylolmethacrylamide, 1,2-ethylene bisacrylamide, 1,4-butane bisacrylamide, and mixtures thereof.

Claim 8

The process of claim 6 wherein the monomer component comprises: a) from about 50 to about 70% by weight of a monomer selected from the group consisting of isodecyl acrylate, n-dodecyl acrylate and 2-ethylhexyl acrylate, and mixtures thereof; b) from about 15 to about 30% by weight of the comonomer selected from the group consisting of styrene, ethyl styrene and mixtures thereof; and c) from about 15 to about 25% by weight of a crosslinking agent selected from the group consisting of divinyl benzene, ethylene glycol dimethacrylate, diethylene glycol dimethacrylate, 1,6-hexanediol diacrylate, 2-butenediol dimethacrylate, ethylene glycol diacrylate, trimethylolpropane triacrylate and trimethacrylate, and mixtures thereof.

Claim 9

The process of claim 2 wherein the polyglycerol aliphatic ethers comprise from about 40 to about 90% linear diglycerol monoaliphatic ethers; and from about 10 to about 60% other polyglycerol ethers.

Claim 10

The process of claim 8 wherein the polyglycerol aliphatic ethers comprise at least about 70% linear diglycerol monoaliphatic ethers.

Claim 11

The process of claim 8 wherein the polyglycerol aliphatic ethers comprise from about 60 to about 95% polyglycerol aliphatic ethers having C 10 -C 24 aliphatic groups.

Claim 12

The process of claim 10 wherein the C 10 -C 24 aliphatic groups are selected from the group consisting of C 12 -C 14 linear saturated aliphatic groups, C 16 -C 24 branched saturated chain aliphatic groups, C 16 -C 22 linear unsaturated aliphatic groups, and mixtures thereof.

Claim 13

The process of claim 11 wherein the C 10 -C 24 aliphatic groups are selected from the group consisting of lauryl, myristyl, isostearyl, 2-octyldodecyl, 2-decyltetradecyl, oleyl, and mixtures thereof.

Claim 14

A process for the preparation of a polymeric foam material, which comprises the steps of: I) forming a water-in-oil emulsion from: A) an oil phase comprising: 1) from about 65 to about 98% by weight of a monomer component capable of forming a polymer having a Tg of about 35° C. or lower and comprising: a) from about 30 to about 85% by weight of at least one substantially water-insoluble monomer having at least one substantially water-insoluble monofunctional monomer capable of forming an atactic amorphous polymer having a Tg of about 25° C. or lower; b) from 0 to about 40% by weight of at least one substantially water-insoluble monofunctional comonomer; and c) from about 5 to about 40% by weight of at least one substantially water-insoluble, polyfunctional crosslinking agent; and 2) from about 2 to about 35% by weight of an emulsifier component which is soluble in the oil phase and which is suitable for forming a stable water-in-oil emulsion, said emulsifier component comprising at least about 40% linear diglycerol monoaliphatic ethers and at least about 60% polyglycerol aliphatic ethers having C 10 -C 24 aliphatic groups; and B) a water phase comprising an aqueous solution containing: 1) from about 0.2 to about 20% by weight of a water-soluble electrolyte; and 2) an effective amount of a polymerization initiator; C) a volume to weight ratio of the water phase to the oil phase in the range of from about 12:1 to about 125:1; II) polymerizing the monomer component in the oil phase of the water-in-oil emulsion to form a polymeric foam material.

Claim 15

A process for the preparation of a polymeric foam material, which comprises the steps of: I) forming a water-in-oil emulsion from: A) an oil phase comprising: 1) from about 65 to about 98% by weight of a monomer component capable of forming a polymer having a Tg of about 35° C. or lower and comprising: a) from about 30 to about 85% by weight of at least one substantially water-insoluble monomer having at least one substantially water-insoluble monofunctional monomer capable of forming an atactic amorphous polymer having a Tg of about 25° C. or lower; b) from 0 to about 40% by weight of at least one substantially water-insoluble monofunctional comonomer; and c) from about 5 to about 40% by weight of at least one substantially water-insoluble, polyfunctional crosslinking agent; and 2) from about 2 to about 35% by weight of an emulsifier component which is soluble in the oil phase and which is suitable for forming a stable water-in-oil emulsion, said emulsifier component comprising at least about 40% linear diglycerol monoaliphatic ethers and at least about 60% polyglycerol aliphatic ethers having C 10 -C 24 aliphatic groups; and B) a water phase comprising an aqueous solution containing: 1) from about 0.2 to about 20% by weight of a water-soluble electrolyte; and 2) an effective amount of a polymerization initiator; C) a volume to weight ratio of the water phase to the oil phase in the range of from about 12:1 to about 125:1; II) polymerizing the monomer component in the oil phase of the water-in-oil emulsion to form a polymeric foam material.

Claim 16

The process of claim 13 comprising the further step of dewatering the polymeric foam material of step II) to an extent such that a collapsed, polymeric foam material is formed that will re-expand upon contact with aqueous fluids.

Claim 17

The process of claim 13 wherein the ratio of the water phase to the oil phase is in the range of from about 20:1 to about 90:1.

Claim 18

The process of claim 15 wherein the ratio of the water phase to the oil phase is in the range of from about 25:1 to about 75:1.

Claim 19

The process of claim 15 wherein the oil phase comprises from about 80 to about 97% by weight monomer component and from about 3 to about 20% by weight emulsifier component.

Claim 20

The process of claim 17 wherein the oil phase comprises from about 90 to about 97% by weight monomer component and from about 3 to about 10% by weight emulsifier component.

Claim 21

The process of claim 17 wherein the monomer component comprises: a) from about 50 to about 70% by weight of a monomer selected from the group consisting of butyl acrylate, hexyl acrylate, octyl acrylate, 2-ethylhexyl acrylate, nonyl acrylate, decyl acrylate, dodecyl acrylate, isodecyl acrylate tetradecyl acrylate, benzyl acrylate, nonylphenyl acrylate, hexyl methacrylate, octyl methacrylate, nonyl methacrylate, decyl methacrylate, isodecyl methacrylate, dodecyl methacrylate, tetradecyl methacrylate, N-octadecyl acrylamide, p-n-octylstyrene, isoprene, 1,3-butadiene, 1,3-hexadiene, 1,3-heptadiene, 1,3-octadiene, 1,3-nonadiene, 1,3-decadiene, 1,3-undecadiene, 1,3-dodecadiene, 2-methyl-1,3-hexadiene, 6-methyl-1,3-heptadiene, 7-methyl-1,3-octadiene, 1,3,7-octatriene, 1,3,9-decatriene, 1,3,6-octatriene, 2,3-dimethyl-1,3-butadiene, 2-amyl-1,3-butadiene, 2,6-dimethyl-1,3,7-octatriene, 2,7-dimethyl-1,3,7-octatriene, 2,6-dimethyl-1,3,6-octatriene, 2,7-dimethyl-1,3,6-octatriene, 7-methyl-3-methylene-1,6-octadiene, 2,6-dimethyl-1,5,7-octatriene, 1-methyl-2-vinyl-4, 6-hepta-dieny-3,8-nonadienoate, 5-methyl-1,3,6-heptatriene, 2-ethylbutadiene, and mixtures thereof; b) from about 5 to about 40% by weight of comonomer selected from the group consisting of styrene, ethyl styrene, methyl methacrylate, and mixtures thereof, and c) from about 10 to about 30% by weight of a crosslinking agent selected from the group consisting of divinylbenzenes, divinyltoluenes, divinylxylenes, divinylnaphthalenes divinylalkylbenzenes, divinylphenanthrenes, trivinylbenzenes, divinylbiphenyls, divinyldiphenylmethanes, divinylbenzyls, divinylphenylethers, divinyldiphenylsulfides, divinylfurans, divinylsulfone, divinylsulfide, divinyldimethylsilane, 1,1'-divinylferrocene, 2-vinylbutadiene, ethylene glycol dimethacrylate, neopentyl glycol dimethacrylate, 1,3-butanediol dimethacrylate, diethylene glycol dimethacrylate, hydroquinone dimethacrylate, catechol dimethacrylate, resorcinol dimethacrylate, triethylene glycol dimethacrylate, polyethylene glycol dimethacrylate, trimethylolpropane trimethacrylate, pentaerythritol tetramethacrylate, 1,4-butanediol dimethacrylate, 1,6-hexanediol diacrylate, 1,4-butanediol diacrylate, tetramethylene diacrylate, trimethyolpropane triacrylate, pentaerythritol tetraacrylate, N-methylolacrylamide, N-methylolmethacrylamide, 1,2-ethylene bisacrylamide, 1,4-butane bisacrylamide, and mixtures thereof.

Claim 22

The process of claim 19 wherein the monomer component comprises: a) from about 50 to about 70% by weight of a monomer selected from the group consisting of isodecyl acrylate, n-dodecyl acrylate and 2-ethylhexyl acrylate, and mixtures thereof; b) from about 15 to about 30% by weight of comonomer selected from the group consisting of styrene, ethyl styrene, and mixtures thereof; and c) from about 15 to about 25% by weight of a crosslinking agent selected from the group consisting of divinyl benzene, ethylene glycol dimethacrylate, diethylene glycol dimethacrylate, 1,6-hexanediol diacrylate, 2-butenediol dimethacrylate, ethylene glycol diacrylate, trimethylolpropane triacrylate and trimethacrylate, and mixtures thereof.

Claim 23

The process of claim 15 wherein the polyglycerol aliphatic ethers comprise from about 40 to about 90% linear diglycerol monoaliphatic ethers; and from about 10 to about 60% other polyglycerol ethers.

Claim 24

The process of claim 21 wherein the polyglycerol aliphatic ethers comprise at least about 70% linear diglycerol monoaliphatic ethers.

Claim 25

The process of claim 21 wherein the polyglycerol aliphatic ethers comprise from about 60 to about 95% polyglycerol aliphatic ethers having C 10 -C 24 aliphatic groups.

Claim 26

The process of claim 23 wherein the C 10 -C 24 aliphatic groups are selected from the group consisting of C 12-C 14 linear saturated aliphatic groups, C 16 -C 24 branched saturated chain aliphatic groups, C 16 -C 22 linear unsaturated aliphatic groups, and mixtures thereof.

Claim 27

The process of claim 24 wherein the C 10 -C 24 aliphatic groups are selected from the group consisting of lauryl, myristyl, isostearyl, 2-octyldodecyl, 2-decyltetradecyl, oleyl, and mixtures thereof.