Dry-blendable solution rubber powders and process

Claim 2

Process for preparing homogeneous, storage-stable, dry-blendable, hydrocarbon solution non-polar rubber powder having a DSV from about 1.5 to about 7.0 (100 parts) containing carbon black, said process being carried out by sequentially (1) grinding carbon black (60-90 phr) in water (2) mixing at a temperature of 20°-100° C., the composition resulting from said (1) with a hydrocarbon solution of rubber, about 5-25% (w/w), to form a liquid two phase dispersion of (a) hydrocarbon, solvent, carbon black, and rubber, and (b) water; (3) stripping the liquid dispersion of said (2) of solvent by adding, at a rate of between about 360-1270 g./min., said dispersion to vigorously stirred hot water (85-120° C.) in the presence of at least one foam inhibiting surfactant selected from the group consisting of (a) nonionic polyether alcohols with blocked terminal hydroxyl group (0.01-5.0 phr), and, (b) cationic tetraalkylammonium salts having more than 25 carbon atoms in the cation of said salt (0.01-5.0 phr), to produce powder, (4) drying said powder to produce a homogeneous, clean and free-flowing powder having a mean particle size from 0.8 to 1.5 mm., with about one-half of said particles having a particle size greater than 1.0 mm.

Claim 3

Process for preparing homogeneous, storage-stable and dry-blended totally compounded rubber powder in which process, (A) a homogeneous, storage-stable, dry-blendable, hydrocarbon solution non-polar rubber powder having a DSV of from about 1.5 to about 7.0 (100 parts) containing carbon black is prepared by sequentially (1 ) grinding carbon black (60-90 phr) in water, (2) mixing the composition resulting from said (1) with a hydrocarbon solution of rubber to form a two phase liquid dispersion of (a) hydrocarbon solvent, carbon black, and rubber, and (b) water, (3) stripping the liquid dispersion of said (2) of solvent by adding said dispersion to vigorously stirred hot water (85-120° C.) in the presence of at least one foam inhibiting surfactant selected from the group consisting of (a) nonionic polyether alcohols with blocked terminal hydroxyl group (0.01-5.0 phr), and, (b) cationic tetraalkylammonium salts having more than 25 carbon atoms (0.01-5.0 phr), to produce powder, (4) drying the powder of said step (3) to produce a homogeneous, clean and free-flowing powder having a mean particle size from about 0.8 to about 1.5 mm., with about half of said particles having a particle size greater than 1.0 mm., followed by, (B) dry-blending, powder compounding, for about 2.5 to about 3.5 min. at 1000-5000 r.p.m., the solution powder product of said (A) with from about 45 to about 60 phr oil, and, from about 0.1 to about 20 phr, collectively, of at least one pigment, at least one preservative and at least one curative, to produce said totally compounded rubber powder.

Claim 4

Process for preparing homogeneous, storage-stable and dry-blended totally compounded rubber powder in which process, (A) a homogeneous, storage-stable, dry-blendable, hydrocarbon solution non-polar rubber powder having a DSV of from about 1.5 to about 7.0 (100 parts) containing carbon black is prepared by sequentially (1 ) grinding carbon black (60-90 phr) in water, (2) mixing the composition resulting from said (1) with a hydrocarbon solution of rubber to form a two phase liquid dispersion of (a) hydrocarbon solvent, carbon black, and rubber, and (b) water, (3) stripping the liquid dispersion of said (2) of solvent by adding said dispersion to vigorously stirred hot water (85-120° C.) in the presence of at least one foam inhibiting surfactant selected from the group consisting of (a) nonionic polyether alcohols with blocked terminal hydroxyl group (0.01-5.0 phr), and, (b) cationic tetraalkylammonium salts having more than 25 carbon atoms (0.01-5.0 phr), to produce powder, (4) drying the powder of said step (3) to produce a homogeneous, clean and free-flowing powder having a mean particle size from about 0.8 to about 1.5 mm., with about half of said particles having a particle size greater than 1.0 mm., followed by, (B) dry-blending, powder compounding, for about 2.5 to about 3.5 min. at 1000-5000 r.p.m., the solution powder product of said (A) with from about 45 to about 60 phr oil, and, from about 0.1 to about 20 phr, collectively, of at least one pigment, at least one preservative and at least one curative, to produce said totally compounded rubber powder.