间接蒸汽加热时二元连续精馏塔提馏段操作线方程

Discussion about Operating Line Equation of Stripping Section for Two continent Contineously Operating Rectification Tower with Indirect Steam Heater

提出了间接蒸汽加热时二元连续精馏塔以ｘＦ、ｘＤ、ｘＷ、ｑ。

This paper presents the stripping stage operating line equation of the two component continuous rectification tower with interface heat exchanger in bottom. The equation is expressed by parameters such as x F、x D、x W、q、R and α.