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This document summarizes a study that used process simulation software to model and analyze crude oil distillation. The study performed steady state simulations of a crude distillation unit with different heat exchanger arrangements. Four cases were simulated: 1) without a preheat train, 2) with a preheat train in series with the distillation column, 3) with a preheat train in parallel with partial vaporization, and 4) optimized design with maximum heat recovery. The simulations analyzed heat duties, temper

Author

Hoàng Nhân

Language

EN