摘要
提出了直接蒸汽加热时二元连续精馏塔以xF、xD、xW、q、R表达的提馏段操作线方程,并对直接蒸汽加热和间接蒸汽加热时的提馏段操作线方程进行了讨论和比较.
This paper presents the stripping stage operating line equation of two component continuous rectification tower with direct steam injection. The equation is expressed with such parameters as x F、x D、x * W q and R. The anthors discuss the presented equation and compare it with the equation of rectification tower which has interface heat exchanger in bottom.
关键词
操作线方程
提馏段
精馏塔
直接蒸汽加热
rectification
operating line equation
stripping stage
theoretical tower plate number