A grafting process after solution polymerization
A solution and process technology, which is applied in the field of grafting process after solution polymerization, can solve the problems of difficult solvent recovery, limited wide application, and long reaction time, and achieves the effects of low price, improved grafting efficiency, and simple operation
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Embodiment 1
[0024] For ethylene-butene polymerization, cyclohexane is used as solvent, and the specific post-treatment process is as follows:
[0025] The ethylene-butene copolymer solution from the polymerization tank first enters the reaction termination unit, where a small amount of soft water is added at the same time to terminate the reaction and deactivate the residual catalyst. The polymer solution coming out of the reaction termination unit goes through the deashing unit to remove catalyst residues and acidic substances, and then enters the grafting unit, where the deashing unit is a column filled with activated alumina or molecular sieve. The grafting unit consists of a stirred reactor, a polymer solution tank and a 30-meter pipe reactor. The polymer solution enters the stirred reactor and the polymer solution tank respectively in two ways, wherein the polymer solution tank is fed continuously, while the stirred reactor is fed intermittently. Add dicumyl peroxide and maleic anhy...
Embodiment 2
[0027] Ethylene-propylene polymerization reaction, using hexane as solvent, the specific post-grafting process is:
[0028] The ethylene-propylene copolymer solution coming out of the polymerization tank first enters the reaction termination unit, where a small amount of steam is added at the same time to terminate the reaction and deactivate the residual catalyst. The polymer solution coming out of the reaction terminating unit enters the grafting unit. The grafting unit consists of a stirred reaction tank and two polymer solution tanks. The polymer solution enters the stirred reactor and the 1# polymer solution tank respectively in two ways, wherein the polymer solution tank is fed continuously, while the stirred reactor is fed intermittently. The 2# polymer solution tank has always maintained a certain amount of polymer solution, and the storage capacity is equivalent to the feed amount of the stirred reactor. Add dicumyl peroxide and acrylic acid under the condition that...
Embodiment 3
[0030] Ethylene polymerization (branched or hyperbranched polyethylene) reaction, using hexane as a solvent, the specific post-treatment process is:
[0031]The branched or hyperbranched polyethylene solution from the polymerization tank first enters the reaction termination unit, where a small amount of soft water is added at the same time to terminate the reaction and deactivate the residual catalyst. The polymer solution coming out of the reaction termination unit goes through the deashing unit to remove catalyst residues and acidic substances, and then enters the grafting unit, where the deashing unit is a column filled with activated alumina or molecular sieve. The grafting unit consists of a stirring reaction tank and a polymer solution tank. The polymer solution enters the stirred reactor and the polymer solution tank respectively in two ways, wherein the polymer solution tank is fed continuously, while the stirred reactor is fed intermittently. Add dibenzoyl peroxide ...
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