Effect of dispersion on tubular reactor yield for variable density cases
β Scribed by Chee Gen Wan; Edward N. Ziegler
- Publisher
- Elsevier Science
- Year
- 1973
- Tongue
- English
- Weight
- 941 KB
- Volume
- 28
- Category
- Article
- ISSN
- 0009-2509
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β¦ Synopsis
Ah&act-
The effects of dispersion on the yields of consecutive reactions have been studied for variable density and adiabatic situations. Quasilinearization is used to solve the nonlinear boundary value problems. Variable density yields ditfer considerably from those of constant density at equivalent dimensionless space times and reaction velocity ratio. The difference in numerical solutions between constant DL and constant DJv cases is small. The yield loss due to mixing, as measured by the deviation from the ideal plug flow situation, for both constant and variable density cases, is approximately the same order of magnitude. For constant density reactions, the intermediate in competitive consecutive reactions follows a characteristic yield that has similar properties to that for a simple series reaction.
π SIMILAR VOLUMES
The one-dimensional model of an isothermal continuous flow tubular reactor with axial diffusion, considered in part I, is extended to deal with variable temperatures. A differentia equation is deduced which allows the optimum yields and optimum temperature. distributions to be determined. Some numer