Modeling of chemical reactors—XXVII. Steady state axial heat and mass transfer in tubular reactors. Effect of different values of Peclet numbers on the region of multiplicity
- 9 October 1973
- journal article
- Published by Elsevier in Chemical Engineering Science
- Vol. 28 (10), 1897-1900
- https://doi.org/10.1016/0009-2509(73)85073-0
Abstract
No abstract availableThis publication has 3 references indexed in Scilit:
- Packed bed axial thermal conductivityChemical Engineering Science, 1972
- Modeling of chemical reactors — XVII Steady state axial heat and mass transfer in tubular reactors Numerical investigation of multiplicityChemical Engineering Science, 1970
- Modeling of chemical reactors — XVI Steady state axial heat and mass transfer in tubular reactors An analysis of the uniqueness of solutionsChemical Engineering Science, 1970