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Loop construction ethylene

Aside from process comparisons, the main contrast between the systems is that of size, weight, and cost, especially for pressurized systems. Construction of batch reactors for use with ethylene at pressures of 1000 psi (70 atm) and upward has to be massive. The simple construction of the Loop process just pumps and pipework blends itself to use at high pressures. Apart from cost and weight, the small volume of the Loop reactor has obvious safety advantages. Despite these attractions, the Loop reactor system has so far been used successfully only for low-pressure systems such as poly(vinyl acetate) homopolymer for adhesives and copolymers for paint. Large-scale production of ethylene-vinyl acetate copolymers has yet to be demonstrated. [Pg.716]

The construction of calix-crown molecules is achieved by grafting ethylene glycol chains in a loop at two of the phenolic functions (Fig. 3A). [Pg.139]


See other pages where Loop construction ethylene is mentioned: [Pg.71]    [Pg.71]    [Pg.82]    [Pg.92]    [Pg.137]    [Pg.82]    [Pg.650]   
See also in sourсe #XX -- [ Pg.472 , Pg.473 ]




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