Abstract A method for removing at least a portion of dissolved gases from a liquid dispersion utilizing a closed, cylindrical tower with an inlet in its upper portion, a tank at the bottom of the tower for collecting liquids, a central pipe in the tower open at each end, the upper end extending above the inlet and the lower end terminating above the level of the collected liquids in the tank and a plurality of inclined surfaces mounted around the central pipe and providing a flow path for the dispersion, each of the plurality of inclined surfaces being shaped and positioned to reverse the direction of flow and dimensioned to form an annular gap between the inclined surfaces and the wall of the tower, the inclined surfaces forming an angle of about 45° to 80° with the central pipe.
A process for lowering the gaseous monomer content of solid-liquid dispersions obtained during the manufacture of polyvinyl chloride according to the suspension or emulsion method, comprising the steps of: flowing the dispersion over a succession of inclined surfaces forming an angle of about 45° to 80° with the vertical at temperatures of about 30°-90° C in a layer thickness of about 0.5 - 5 mm during a period of about 2-20 seconds; collecting the remaining dispersion and the gaseous phase of the monomers liberated by the flowing step; and removing the thus-liberated gaseous monomer directly from the interface between the dispersion and the gaseous phase of the monomers.
Claim 2
Dependent Claim
108 words
A process for lowering the gaseous monomer content of solid-liquid dispersions obtained during the manufacture of polyvinyl chloride according to the suspension or emulsion method, comprising the steps of: flowing the dispersion over a succession of inclined surfaces forming an angle of about 45° to 80° with the vertical at temperatures of about 30°-90° C in a layer thickness of about 0.5 - 5 mm during a period of about 2-20 seconds; collecting the remaining dispersion and the gaseous phase of the monomers liberated by the flowing step; and removing the thus-liberated gaseous monomer directly from the interface between the dispersion and the gaseous phase of the monomers.
Claim 3
Dependent Claim
24 words
The process of claim 1, wherein the flowing step includes the step of maintaining an absolute pressure of 30-700 mbar during the flowing step.
Claim 4
Dependent Claim
29 words
The process of claim 2, wherein the flowing step includes the step of reversing the direction of flow of the dispersion at each of said succession of inclined surfaces.
Claim 5
Dependent Claim
52 words
The process of claim 3, wherein the dispersion is flowed over inclined surfaces forming an angle of about 75° with the vertical at a temperature of about 75° C, at an absolute pressure of about 375 mbar with a layer thickness of about 1.0 mm during a period of about 10 seconds.