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2 ( 2 0 ) . You are tasked with improving the bed efficiency, , of a fixed - bed adsorption process from an unacceptable

2(20). You are tasked with improving the bed efficiency, , of a fixed-bed adsorption process from an unacceptable value of 0.67 to the target value of 0.80. The target solute feed is dilute and at fixed concentration, cF. A linear isotherm applies, q=Kc, and the breakthrough curve is described well by an expression based on the error function, erf (see below). Although the economical breakthrough concentration has not been established yet, an approximate process time corresponding to the midpoint of the breakthrough curve, t0, at =0.7 has been set. Also, solution composition and temperature have been set, so K cannot be manipulated.
(a) Given the conditions described above and prior knowledge that the separation is limited by internal diffusion, what parameter(s) can be manipulated and in what manner (up or down) to improve given fixed, CF,t0 and K? Note the table below as well as the expressions for , the breakthrough curve, and the slope of the breakthrough curve at t=t0. The expression for the slope is valid for any breakthrough curve described using the expression based on erf.
(b) Determine quantitatively the change in one or more parameters to improve to 0.80 given the constraints described in the problem statement above.
=2tBtE+tB=1-tE-tBtE+tB,ccF=12(1+erf[t-to22to]),( slope @to)=0.399cFto
\table[[Controlling,2 is,to is,NTU is,R is],[Step,proportional to,proportional to,proportional to,proportional to]]
Internal Diff'n ,vd2L,dLv2,Lvd2,1dLv2
Ext. Transport ,v12d32L,L12d34v34,Lv12d32,L12d34v14
Dispersion ,vd2L,dLv2,Lvd2,1dLv2
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