Process for treating latices

Claim 2

A process for removing unreacted monomers or solvents from a latex selected from the group consisting of synthetic rubber latex and synthetic resin latex which comprises bringing said latex into contact with an inert gas fluid, without imposition of any substantial mechanical shear stress, at a temperature ranging from 20° to 100° C by feeding said latex into the upper part of an wetted-wall tower (falling film evaporator), said wetted-wall tower being provided with one or a plurality of circular tubes opened at the both ends and standing vertically, the latex being supplied at the upper end of the tube so as to contact with tube walls, the feed rate of latex being the range of from 5 to 100 gm/min/cm perimeter, the latex fed being caused to flow down spontaneously by gravity along tube walls in the state of film, the average thickness of said film being in the range of from 0.2 to 1.2 mm and an inert gas being introduced into said tubes at the lower or upper part of said tubes.

Claim 3

A process as claimed in claim 1 in which said latex is an emulsion containing a polymer selected from the group consisting of butadiene rubber, butadiene-styrene rubber, butadiene-acrylonitrile rubber, polyvinylchloride, polyvinylacetate, ethylene-vinylacetate copolymer, polystyrene and polychloroprene.

Claim 4

A process as claimed in claim 1 in which said wetted-wall tower contains a plurality of vertical tubes each tube of which has an inner diameter of from 5 to 150 mm and a tubular length of from 2 to 20 m.

Claim 5

A process as claimed in claim 1 in which said inert gas is a member selected from the group consisting of air and nitrogen.

Claim 6

A process for removing unreacted monomers from an emulsion obtained at a stage in which polymerization steps have been completed in the production of butadiene rubber, styrene-butadiene rubber, butadiene-acrylonitrile rubber, polyvinyl acetate, polyvinyl chloride, ethylene-vinyl acetate copolymer, polystyrene, polychloroprene and latex thereof by emulsion polymerization which consists essentially of bringing said emulsion into contact with an inert gas fluid, without imposition of any substantial mechanical shear stress, at a temperature ranging from 40° to 100° C by feeding the said latex into the upper part of a wetted-wall tower (falling film evaporator), said wetted-wall tower being provided with one or a plurality of circular tubes opened at the both ends and standing vertically, the latex being supplied at the upper end of the tube so as to contact with tube walls, the feed rate of latex being in the range of from 5 to 100 gm/min/cm perimeter, the latex fed being caused to flow down spontaneously by gravity along tube walls in the state of film, the average thickness of said film being in the range of from 0.2 to 1.2 mm and an inert gas being introduced into said tubes at the lower or upper part of said tubes.

Claim 7

A process for removing unreacted monomers from an emulsion obtained at a stage in which polymerization steps have been completed in the production of butadiene rubber, styrene-butadiene rubber, butadiene-acrylonitrile rubber, polyvinyl acetate, polyvinyl chloride, ethylene-vinyl acetate copolymer, polystyrene, polychloroprene and latex thereof by emulsion polymerization which consists essentially of bringing said emulsion into contact with an inert gas fluid, without imposition of any substantial mechanical shear stress, at a temperature ranging from 40° to 100° C by feeding the said latex into the upper part of a wetted-wall tower (falling film evaporator), said wetted-wall tower being provided with one or a plurality of circular tubes opened at the both ends and standing vertically, the latex being supplied at the upper end of the tube so as to contact with tube walls, the feed rate of latex being in the range of from 5 to 100 gm/min/cm perimeter, the latex fed being caused to flow down spontaneously by gravity along tube walls in the state of film, the average thickness of said film being in the range of from 0.2 to 1.2 mm and an inert gas being introduced into said tubes at the lower or upper part of said tubes.

Claim 8

A process as claimed in claim 5 in which said wetted-wall tower contains a plurality of vertical tubes each tube of which has an inner diameter of from 5 to 150 mm and a tube length of from 2 to 20 mm.

Claim 9

A process as claimed in claim 5 in which said inert gas is a member selected from the group consisting of air and nitrogen.