A two-phase approach was used for the optimization of a propylene chlorohydrin reactor in a 10, 000 t/year propylene oxide plant based on a simplified steady-state model.

• 以10，000吨／年环氧丙烷装置氯醇化反应工段为对象，采用简化的机理模型，通过两相法实施过程的操作优化。