Production of a powder of polyvinylchloride or a vinylchloride copolymerizate suitable for producing plastisols

Claim 2

A drying tower comprising a tower having a cylindrical part, means at one end thereof for providing a flow of drying air through the tower, at least one two-fluid nozzle for atomizing liquid into the tower by means of pressurised air in which the pressurised air is projected annularly with respect to the liquid, and at least one injector member for injecting air in a direction which, projected onto a plane at right angles to the longitudinal axis of the tower, forms at angle with a line through the centre of the tower and the outlet opening of the injector member, thereby providing within said drying tower a controlled rotary motion of the particles produced by the atomization and the flow of drying air.

Claim 3

A drying tower for use in performing the process as claimed in claim 1 comprising a tower having a cylindrical part, means at one end thereof for providing a flow of drying air through the tower, and at least one two-fluid nozzle for atomizing liquid into the tower by means of pressurised air, at least one such two-fluid nozzle being so directed that its centre line, projected onto a plane at right angles to the longitudinal axis of the towwr, forms an angle (δ) with a line also projected onto said plane through the centre of the tower and the outlet orifice of the nozzle, or being arranged for being turned so that the centre line projected onto said plane forms an angle with said line (projected onto said plane).

Claim 4

A powder obtained as a result of the process in accordance with claim 1.

Claim 5

A process for the production of a powder of polyvinylchloride or a vinylchloride copolymerisate suitable for the production of plastisols comprising (a) atomizing an aqueous dispersion of polyvinylchloride or a vinylchloride copolymerisate into a substantially uniform flow of drying air within a drying tower, so that the drying is carried out substantially as a co-current process, said atomizing taking place via at least one two-fluid nozzle in which pressurised air is projected annularly with respect to said aqueous dispersion of polyvinylchloride or vinylchloride copolymerisate, (b) providing within said drying tower a controlled rotary motion of particles produced by the atomization and of the drying air about the longitudinal axis of said drying tower by injecting, via at least one injection member, pressurised air in a direction which, projected onto a plane at right angles to the longitudinal axis of the drying tower, forms an angle with a line through the centre of the drying tower and the injector outlet orifice, and (c) grinding at least the coarsest fraction of the resulting powder.

Claim 6

A process for the production of a powder of polyvinylchloride or a vinylchloride copolymerisate suitable for the production of plastisols comprising (a) atomizing an aqueous dispersion of polyvinylchloride or a vinylchloride copolymerisate into a substantially uniform flow of drying air within a drying tower, so that the drying is carried out substantially as a co-current process, said atomizing taking place via at least one two-fluid nozzle in which pressurised air is projected annularly with respect to said aqueous dispersion of polyvinylchloride or vinylchloride copolymerisate, (b) providing within said drying tower a controlled rotary motion of particles produced by the atomization and of the drying air about the longitudinal axis of said drying tower by injecting, via at least one injection member, pressurised air in a direction which, projected onto a plane at right angles to the longitudinal axis of the drying tower, forms an angle with a line through the centre of the drying tower and the injector outlet orifice, and (c) grinding at least the coarsest fraction of the resulting powder.

Claim 7

A process as claimed in claim 1, wherein the temperature of the drying air, when introduced into the drying tower, is above 140° C.

Claim 8

A process as claimed in claim 5, wherein the temperature of the drying air, when introduced into the drying tower, is between 180° and 280° C.

Claim 9

A process as claimed in claim 1, wherein at least one two-fluid nozzle is used as the injector member.

Claim 10

A process as claimed in claim 1, wherein a plurality of two-fluid nozzles are used and the direction of said two-fluid nozzles is so adjusted that the angle formed between the centre line of each nozzle and a line through the centre of the drying tower and the orifice of the nozzle, projected onto a plane at right angles to the longitudinal axis of the tower is different for the individual two-fluid nozzles or groups of two-fluid nozzles.

Claim 11

A process as claimed in claim 1, wherein a plurality of two-fluid nozzles are used and some of the two-fluid nozzles are so adjusted that their centre lines form an angle with a line through the centre of the drying tower and the orifice of the nozzles, projected onto a plane at right angles to the longitudinal axis of the tower, whereas other two-fluid nozzles are so directed that their projected centre lines coincide with said projected line.