Process of making water-absorbent, water-insoluble, cross linked fiber or film

Claim 2

A process of making water-absorbent, water-insoluble, cross linked polymer fibre or film having a gel capacity of at least 50 g deionized water per gram comprising extruding into a gas atmosphere a 5 to 50 weight percent solution in a solvent of a substantially linear polymer formed of a water soluble bend of monoethylenically unsaturated monomers and thereby precipitating the polymer by evaporation of the solvent and forming polymeric fibre or film, stretching the fibre or film and then cross linking the polymer in the stretched fibre or film, and in which the polymer fibre or film is permanently plasticised by inclusion of a plasticising amount of plasticising monomer in the monomer blend and the said solvent comprises an external plasticiser that is dissolved in the polymer of the fibre or film and that plasticises the fibre or film throughout the stretching and that is present in the stretched fibre or film in a plasticising amount and that comprises a volatile liquid, and in which the volatile liquid is evaporated during or after the cross linking.

Claim 3

A process according to claim 1 in which the external plasticiser is solvent from the polymer solution.

Claim 4

A process according to claim 1 in which the polymer solution is an aqueous solution and the external plasticiser comprises water.

Claim 5

A process according to claim 1 in which the amount of external plasticiser in the said stretched fibre or film is at least 10% based on the dry weight of the fibre or film.

Claim 6

A process according to claim 1 in which the stretched fibre or film is substantially non-tacky before it is cross linked and while it still contains the external plasticiser and the drawn fibre or film is collected and is then cross linked.

Claim 7

A process according to claim 1 in which the external plasticiser comprises material that is reactive with the linear polymer and is reacted into the polymer during cross linking.

Claim 8

A process according to claim 1 in which the monomer blend includes 10 to 50% by weight of a plasticising monomer selected from the group consisting of styrenes, vinyl esters, acrylonitrile and alkyl- and hydroxyalkyl- esters of ethylenically unsaturated acids.

Claim 9

A process according to claim 1 in which the monomer blend comprises carboxylic acid monomer and the cross linking is covalent cross linking.

Claim 10

A process according to claim 1 in which cross linking is effected by reaction between the substantially linear polymer and a cross linking reagent dissolved in the polymer solution and which is soluble in the polymer.

Claim 11

A process according to claim 1 in which the cross linking is by reaction between pendant groups derived from different monomers of the monomer blend.

Claim 12

A process according to claim 1 in which the monomer blend comprises monomer that provides carboxylic acid monomer groups and monomer that provides hydroxyl groups that can react with the carboxylic acid groups and the cross linking is by the formation of ester groups between the carboxylic and hydroxylic groups.

Claim 13

A process according to claim 1 in which the polymer is extruded in the form of a fibre.

Claim 14

A process according to claim 1 in which the polymer is extruded in the form of a film.

Claim 15

A process of making water-absorbent, water-insoluble, cross linked polymer fibre or film having a gel capacity of at least 50 g deionized water per gram comprising extruding into a gas atmosphere a 5 to 50 weight percent aqueous solution of a substantially linear polymer formed of a water soluble blend of a monoethylenically unsaturated monomers comprising carboxylic acid monomer and a plasticising amount of a plasticising monomer sufficient to permanently plasticise the fibre or film in a solvent and thereby precipitating the polymer by evaporation of the solvent and forming polymeric fibre or film, stretching the fibre or film to form stretched fibre or film, the water of said solvent comprising an external plasticiser that is dissolved in the polymer of the fibre or film and that plasticises the fibre or film throughout the stretching and that is present in the stretched fibre or film in a plasticising amount of at least 10% based on the dry weight of the fibre or film, collecting substantially non-tacky stretched fibre or film still containing external plasticiser, covalently cross linking the stretched fibre or film, and in which water is evaporated during or after the cross linking.

Claim 16

A process of making water-absorbent, water-insoluble, cross linked polymer fibre or film having a gel capacity of at least 50 g deionized water per gram comprising extruding into a gas atmosphere a 5 to 50 weight percent aqueous solution of a substantially linear polymer formed of a water soluble blend of a monoethylenically unsaturated monomers comprising carboxylic acid monomer and a plasticising amount of a plasticising monomer sufficient to permanently plasticise the fibre or film in a solvent and thereby precipitating the polymer by evaporation of the solvent and forming polymeric fibre or film, stretching the fibre or film to form stretched fibre or film, the water of said solvent comprising an external plasticiser that is dissolved in the polymer of the fibre or film and that plasticises the fibre or film throughout the stretching and that is present in the stretched fibre or film in a plasticising amount of at least 10% based on the dry weight of the fibre or film, collecting substantially non-tacky stretched fibre or film still containing external plasticiser, covalently cross linking the stretched fibre or film, and in which water is evaporated during or after the cross linking.

Claim 17

A process according to claim 14 in which the said blend consists essentially of carboxylic acid monomer and 10 to 50% by weight of a plasticising monomer selected from the group consisting of styrenes, vinyl esters, acrylonitrile and alkyl- and hydroxylalkyl- esters of ethylenically unsaturated acid.

Claim 18

A process according to claim 15 in which the said blend contains 1 to 15% hydroxyalkyl (meth) acrylate.

Claim 19

A process according to claim 16 in which the polymer is extruded in the form of a fibre.

Claim 20

A process according to claim 16 in which the polymer is extruded in the form of a film.