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- W1979510438 abstract "This paper discusses the role of the chemical engineer in the management of energy through process design with particular reference to multicomponent distillation combined with heat exchanger networks.Since there is no analytical solution it is necessary to consider actual cases. Four systems of four components and one of five are considered in detail. Both are near-ideal in their vapour—liquid equilibrium relationships and for each system a wide range of feed compositions is considered for each of two degrees of recovery (90% and 99%). For no heat interchange between streams, it is found that the conventional sequential distillation sequence is the optimum in energy terms for all but four cases. When heat interchange is considered, however, nearly half the four-component cases and one-third of the five-component cases require configurations other than this simple sequential one for minimal energy consumption.The rules suggested by Rathore et al. are shown to be valid in including all feasible matches but do not exclude all non-feasible ones." @default.
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- W1979510438 date "1869-04-01" @default.
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- W1979510438 title "The dredging machine" @default.
- W1979510438 doi "https://doi.org/10.1016/0016-0032(69)90545-6" @default.
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