## Abstrret -Plug flow as well as axml chspersion dynamic models for counter-flow extractwe reactors are formulated and solved to mvesmte the frequency response charactenstuzs of such reactors The reactions considered are taken to he either mfimtely fast, takmg place at the interface between the t
The influence of stoichiometry and excess on the conversion in axial-dispersed tubular flow reactors
✍ Scribed by W. Deckwer; H. Kölbel; L. Langemann
- Publisher
- Elsevier Science
- Year
- 1972
- Tongue
- English
- Weight
- 723 KB
- Volume
- 27
- Category
- Article
- ISSN
- 0009-2509
No coin nor oath required. For personal study only.
✦ Synopsis
The application of the dispersion model of flow reactors for reactions of any order with two reactants and different initial concentrations yields a system of differential equations which can by considering the stoichiometry of the reaction be reduced to one differential equation.
The numerical solution of the differential equation discloses the influence of the stoichiometry and the different initial concentrations on the concentration profiles. For the important case of a Znd-order reaction, diagrams are presented which show the deviation of the concentration when the reaction is treated like a pseudo I St-order reaction. Since for the 1 St-order reaction the reactor outlet concentration can be calculated from the analytical solution, the prepared diagrams offer the possibility to determine the conversion for a 2nd-order reaction rapidly and without employing a computer.
📜 SIMILAR VOLUMES
## Ah&act- The stability of the steady-state conditions in a tubular packed bed reactor with axial diffusion and thermal conduction has been investigated with respect to small perturbations of extent and temperature. The analysis leads to an eigenvalue problem and the stability or instability of t
The effect of different values of Peclet numbers (Pee # Pe,,) on the region of multiplicity in adiabatic tubular reactors is followed. A modification of the mapping technique for this case is proposed. The results of calculation are presented in graphs. For the range of experimentally observed ratio