| 摘要 |
Polymers of alpha-olefins having 2 to 8 carbon atoms in the molecule and containing about 20 to 55% of solvent are processed by forming a disperse phase suspension of the polymer in a heated gaseous suspending medium at a temperature sufficiently high to volatilize the solvent without melting the polymer and flowing the suspension in the disperse phase through a first zone which removes solvent from the polymer in particulate form to give a solvent content of from 2 to about 15%, forming the separated polymer into a first dense fluidized bed with a heated gaseous fluidizing medium at a temperature below the melting-point of the polymer to reduce further the solvent content of the polymer to about 0.05 to 1.5% by weight, then forming this polymer into a second dense fluidized bed with a heated inert gasiform medium at a temperature below the melting point of the polymer and not less than the temperature of the first fluidized bed whereby the solvent content of the polymer is reduced to less than 100 p.p.m. and the polymer recovered from the second bed. The polymers processed may be polyethylene, polypropylene, ethylene-propylene copolymers, ethylene-butene-1 copolymers, or ethylene-pentene-1 copolymers. The polymers are made by using Ziegler-Natta type catalysts and conventional diluents, i.e. hydrocarbons and halogenated aromatic hydrocarbons. The initial solvent in the polymer is generally a mixture of a hydrocarbon and an aliphatic alcohol, e.g. xylene and methanol. The suspending and fluidizing medium may be solvent vapours, natural hydrocarbon gases such as methane, ethane, or propane, inert gases such as nitrogen, and steam at a temperature above the dew point. The Specification also includes a flow diagram of a method for continuously processing the polymers.
|
