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Theoretical step response RTDs and determination of minimal axial dispersion in the experimental layout.

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posted on 2014-04-18, 11:16 authored by Clément de Loubens, Roger G. Lentle, Corrin Hulls, Patrick W. M. Janssen, Richard J. Love, J. Paul Chambers

Left: Theoretical step response RTD for different numbers (n) of continuous stirred tanks reactors (CSTRs) in series. Plug flow reactor (PFR) configuration (no axial but perfect radial mixing) is approached as the number of CSTRs tends to infinity. Right: Experimental step response RTD (plain circles) after passage through a length of silicone rubber tubing of similar dimensions and flow rate to those of the isolated proximal duodenum. The line of best fit was for 68 CSTRs in series (R2 = 0.99, plain line).

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