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Underwood Equations for Minimum Reflux Ratio

The Underwood equations can be used to calculate the minimum reflux ratio in a multicomponent system if the relative volatilities of the components are constant. There are two equations. [Pg.37]

The feed composition Zj (mole fractions j= 1, NC), the desired distillate composition Xpj (/ = 1, NC), and the feed thermal condition q are specified. The relative volatilities ot, (/ = 1, NC) of the multicomponent mixture are known. [Pg.38]

The first equation contains one unknown parameter 6. However, expanding the summation of NC terms and multiplying through all the denominator terms (aj 0) give a polynomial in 6 whose order is NC. Therefore, there are NC roots of this polynomial. One of these roots lies between the two relative volatility values otoc and q hk- This is found using some iterative solution method. It is substituted into the second equation, which can then be solved explicitly for the minimum reflux ratio. [Pg.38]

An example of the use of the Underwood equations is given in Chapter 4. The results of this approximate method will be compared with the results found from rigorous simulation. [Pg.38]

Several methods for analyzing distillation columns have been presented in this chapter. Graphical methods provide valuable insight into how various parameters affect separations in distillation. [Pg.38]


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