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Plug flow (tubular) reactor — Stoli Chem

Plug flow (tubular) reactor — Stoli Chem

The following differential equation describes the steady-state concentration of a substance that reacts with first-order kinetics in an axially-dispersed plug-flow reactor (Fig. P28.14), D (d^2 c)/(d x^2)-U (d c)/(d x)-k c=0 where D= the dispersion coefficient [m^2 / hr], c= concentration [mol / L], x= distance [m], U= the velocity [m / hr] and k= the reaction rate [/ hr] . The boundary conditions can be formulated as U cin=U c(x=0)-D (d c)/(d x)(x=0) (d c)/(d x)(x=L)=0 where cin = the

The following differential equation describes the steady-state concen…

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The reaction, A â†’ B, is to be carried out isothermally in a continuous plug flow reactor. Calculate the volume necessary to consume 99% of A when the entering molar flow rate is 5 mol/h assuming the reaction rate is â€“rA = k with k = 0.05 mol/h.dm^3. The entering volumetric flow rate is 10 dm^3/h.

The reaction, A â†’ B, is to be carried out isothermally in a conti…

The aqueous decomposition of A is studied in an experimental mixed flow reactor. The results in Table P 5.25 are obtained in steady-state runs. To obtain 75 % conversion of reactant in a feed, CA 0=0.8 mol/liter, what holding time is needed in a plug flow reactor? | Numerade

The aqueous decomposition of A is studied in an experimental mixed …

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