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有相对挥发度为2的理想溶液,用板式精馏塔分离。溜出液流量为100mol/h,回流比R=2,测得进入第n板的气液相组成分别为yn+1=0.8、xn-1=0.82,若塔板以气相组成表示的单板效率Emv=0.5,试计算离开第n板的气液两相组成。
A.8、xn-1=0.82,若塔板以气相组成表示的单板效率Emv=0.5,试计算离开第n板的气液两相组成。
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