Claims Analysis
Total Claims: 8
Claim 1
Independent Claim
183 words
A continuous process using a plurality of reaction vessels connected in series for producing arylene sulfide polymer by contacting a dihalo aromatic compound with a sulfur source in an organic amide to produce a particulate polymeric product, said method comprising: a. introducing the reactant compounds into a first reaction vessel maintained at polymerization conditions of temperature and pressure sufficient to remove water and organic amide from the reaction by evaporation thereby producing a reaction mixture; b. introducing effluent reaction mixture from the first reaction vessel to a second reaction vessel maintained at a pressure about 2 Kg/cm 2 below the pressure of the first reactor that flow of reactants is induced from said first reaction vessel to said second reaction vessel, said second reaction vessel maintained at a temperature sufficient to evaporate water and organic amide from the reaction mixture thereby concentrating the reaction mixture in the second reaction vessel; and c. subjecting the effluent reaction mixture from the second reaction vessel to a reduced pressure sufficient to flash evaporate the liquid portion to recover a particulate, polymeric product and a condensible vapor.
Claim 2
Dependent Claim
183 words
A continuous process using a plurality of reaction vessels connected in series for producing arylene sulfide polymer by contacting a dihalo aromatic compound with a sulfur source in an organic amide to produce a particulate polymeric product, said method comprising: a. introducing the reactant compounds into a first reaction vessel maintained at polymerization conditions of temperature and pressure sufficient to remove water and organic amide from the reaction by evaporation thereby producing a reaction mixture; b. introducing effluent reaction mixture from the first reaction vessel to a second reaction vessel maintained at a pressure about 2 Kg/cm 2 below the pressure of the first reactor that flow of reactants is induced from said first reaction vessel to said second reaction vessel, said second reaction vessel maintained at a temperature sufficient to evaporate water and organic amide from the reaction mixture thereby concentrating the reaction mixture in the second reaction vessel; and c. subjecting the effluent reaction mixture from the second reaction vessel to a reduced pressure sufficient to flash evaporate the liquid portion to recover a particulate, polymeric product and a condensible vapor.
Claim 3
Dependent Claim
73 words
The method of claim 1 wherein effluent from the second reaction vessel is introduced into a third reaction vessel in which the pressure is reduced about 2 Kg/cm 2 below that of the second reaction vessel to induce flow of effluent from the second reaction vessel to the third reaction vessel and subjecting the effluent from the third reaction vessel to flash evaporation to recover a particulate, polymeric product and a vaporized liquid.
Claim 4
Dependent Claim
29 words
The method of claim 1 wherein the temperature of the second reaction vessel is increased about 5° C to about 20° C above that of the first reaction vessel.
Claim 5
Dependent Claim
53 words
The method of claim 2 wherein the temperature in the second reaction vessel is increased about 5° C to about 20° C above that of the first reaction vessel and the temperature of the third reaction vessel is increased about 5° C to about 20° C above that of the second reaction vessel.
Claim 6
Dependent Claim
14 words
A method of claim 1 wherein the reactant compounds comprise a polymerization modifying compound.
Claim 7
Dependent Claim
40 words
A method of claim 1 wherein the polymerization conditions comprise reaction temperature within the range of about 125° C to about 450° C and reaction pressure in the range of about 1 Kg/cm 2 to about 20 Kg/cm 2 .
Claim 8
Dependent Claim
32 words
A method of claim 6 wherein the reaction temperature is about 175° C to about 350° C and the reaction pressure is about 5 Kg/cm 2 to about 18 Kg/cm 2 .