Process for production of high to ultra-high molecular weight linear polyarylenesulfides

Claim 2

A process for producing a high molecular to ultra-high molecular weight linear polyarylenesulfide, which comprises: providing a prepolymer which is an arylenesulfide polymer having a melt viscosity of 5 to 3,000 poise measured at 310° C. and a shear rate of 200 sec -1 ; placing the prepolymer in a solvent which consists essentially of a strongly alkaline mixture of an organic amide and 7 to 30% by weight of water; heating said prepolymer in said solvent at a temperature of from 245° to 290° C., whereby a mass is formed in a liquid-liquid two phase state wherein the prepolymer is present mostly in one of the two phases; maintaining the liquid-liquid two-phase state for 1 to 50 hours thereby to convert the prepolymer into an arylenesulfide polymer of a higher molecular weight; and recovering the arylenesulfide polymer of a higher molecular weight, the alkalinity of said strongly alkaline mixture being such that when diluted 10-fold with water, the pH thereof is 9.5 to 14.

Claim 3

the process according to claim 1, wherein said prepolymer is an arylene sulfide polymer wherein the arylenesulfide moiety is at least one member selected from the group consisting of a p-arylenesulfide moiety and an m-arylenesulfide moiety.

Claim 4

The process according to claim 1, wherein said alkalinity is attained by the addition, to the solvent, of at least one member selected from the group consisting of an alkali metal alcoholate, an alkali metal phenolate, an alkali metal hydroxide, an alkali metal oxide and an alkali metal carbonate.

Claim 5

A process for producing a high molecular weight to ultra-high molecular weight linear polyarylenesulfide, which comprises: heating an alkali metal sulfide and a dihalo-armoatic compound in an organic amide containing 0.5 to 2.4 moles of water per mole of the alkali metal sulfide charged, at a temperature of from 180° C. to 240° C., until an arylenesulfide polymer having a melt viscosity of 5 to 300 poise determined at 310° C. and a shear rate of 200 sec -1 is formed with a conversion of the dihalo-aromatic compound of 70 to 98 mole % thereby form a prepolymer in a reaction mixture; adding additional water to the reaction mixture thus formed in a quantity of 2.5 to 7.0 moles per mole of the alkali metal sulfide charged; and heating the reaction mixture thus formed at a temperature of from 245° C. to 290° C. under strongly alkaline conditions, whereby a mass is formed in a liquid-liquid two phase state wherein the prepolymer is present mostly in one of the two phases; maintaining the liquid-liquid two-phase state for 1 to 50 hours thereby to convert the prepolymer into an arylenesulfide polymer of a higher molecular weight; and recovering the arylenesulfide polymer of a higher molecular weight, said strongly alkaline conditions being such that the pH of the reaction mixture when diluted 10-fold, is from 9.5-14.

Claim 6

A process for producing a high molecular weight to ultra-high molecular weight linear polyarylenesulfide, which comprises: heating an alkali metal sulfide and a dihalo-armoatic compound in an organic amide containing 0.5 to 2.4 moles of water per mole of the alkali metal sulfide charged, at a temperature of from 180° C. to 240° C., until an arylenesulfide polymer having a melt viscosity of 5 to 300 poise determined at 310° C. and a shear rate of 200 sec -1 is formed with a conversion of the dihalo-aromatic compound of 70 to 98 mole % thereby form a prepolymer in a reaction mixture; adding additional water to the reaction mixture thus formed in a quantity of 2.5 to 7.0 moles per mole of the alkali metal sulfide charged; and heating the reaction mixture thus formed at a temperature of from 245° C. to 290° C. under strongly alkaline conditions, whereby a mass is formed in a liquid-liquid two phase state wherein the prepolymer is present mostly in one of the two phases; maintaining the liquid-liquid two-phase state for 1 to 50 hours thereby to convert the prepolymer into an arylenesulfide polymer of a higher molecular weight; and recovering the arylenesulfide polymer of a higher molecular weight, said strongly alkaline conditions being such that the pH of the reaction mixture when diluted 10-fold, is from 9.5-14.

Claim 7

The process according to claim 4, wherein the dihalo-aromatic compound comprises at least one member selected from the group consisting of a p-dihalobenzene and a m-dihalobenzene.

Claim 8

The process according to claim 4, wherein the strongly alkaline condition is attained by the addition, to the solvent, of at least one member selected from the group consisting of an alkali metal alcoholate, an alkali metal phenolate, an alkali metal hydroxide, an alkali metal oxide and an alkali metal carbonate.

Claim 9

The process according to claim 1, wherein said prepolymer is a wet product obtained by the reaction of an alkali metal sulfide with a dihalo-aromatic compound in an organic amide containing a lower quantity of water per mole of the alkali metal sulfide charged, at a temperature of 180° C. to 290° C., until an arylenesulfide polymer having a melt viscosity of 100 to 3,000 poise is formed, separating the polymer, and washing the polymer with a non-oxidative alkali solution.

Claim 10

The process according to claim 1, wherein said prepolymer is a dry product of a polyarylenesulfide having a melt viscosity of 5 to 3,000 poise which has been produced by the reaction of an alkali metal sulfide and a dihaloaromatic compound in a solvent, followed by separating the polymer thus produced, washing of the polymer with a non-oxidative alkali solution and drying.

Claim 11

The process according to claim 7, wherein the non-oxidative alkali solution is an aqueous solution with a pH of 10 to 14 containing at least one member selected from the group consisting of an alkali metal sulfide, an alkali metal alcoholate, an alkali metal phenolate, an alkali metal hydroxide, an alkali metal oxide and an alkali metal carbonate.

Claim 12

The process according to claim 4, wherein the strongly alkaline condition is attained solely by the alkalinity inherent in the previous step.

Claim 13

The process according to claim 1, wherein the organic amide is N-methylpyrrolidone.

Claim 14

The process according to claim 4, wherein the organic amide is N-methylpyrrolidone.

Claim 15

The process according to claim 8, wherein the non-oxidative alkali solution is an aqueous solution with a pH of 10 to 14 containing at least one member selected from the group consisting of an alkali metal sulfide, an alkali metal alcoholate, an alkali metal phenolate, an alkali metal hydroxide, an alkali metal oxide and an alkali metal carbonate.

Claim 16

The process according to claim 4, wherein the quantity of the organic amide is from 0.2 to 5 liters per mole of the metal sulfide employed.

Claim 17

The high molecular weight linear polyphenylenesulfide produced by the process of claim 1.

Claim 18

The high molecular weight linear polyphenylenesulfide produced by the process of claim 4.

Claim 19

A high molecular weight linear polyphenylenesulfide which has a melt viscosity of at least 7,000 measured at a temperature of 310° C. under a shear rate of 200 sec -1 and is substantially free of a cross-linked structure.

Claim 20

A high molecular weight linear polyphenylenesulfide which has a melt viscosity of at least 7,000 measured at a temperature of 310° C. under a shear rate of 200 sec -1 and is substantially free of a cross-linked structure.