Shorter Commumcafions chemical reactron, however, the absorbed gas reacts upon dlssolvrng m the hqmd, and the dnvmg force wdl be considerable also m the semi-stagnant zones, which will contnbute conslderably to the overall mass transfer rate The interfacIal area was measured m three of the tested pa
Experimental observations of multiple steady states in an adiabatical catalytic reactor
✍ Scribed by V. Hlaváček; J. Votruba; H. Hofmann
- Publisher
- Elsevier Science
- Year
- 1976
- Tongue
- English
- Weight
- 156 KB
- Volume
- 31
- Category
- Article
- ISSN
- 0009-2509
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📜 SIMILAR VOLUMES
NOTATION numencal coefficient (subscnpt refers to the equation where It IS defined) drop dmmeter, m maxlmum drop dmmeter, m Sauter mean drop dmmeter, m Impeller diameter, m Impeller speed, s-' power mput to the unpeller, W power mput per umt mass, W kg-' power Input Per umt mass m the volume swept b
The effects of axial heat transfer in fully-insulated reactors and for insulated reactors with heatsink inlets are examined for various model systems with either constant or variable rates of heat evolution along the reactor. Significant departures from adiabatic temperature. profiles arc calculated
## Abstract A model of an adiabatic continuously stirred‐tank reactor in which a single exothermic second order‐gas liquid reaction occurs has been developed. The interactions between the rate of the chemical reaction, the diffusional resistances, and the solubility may cause the occurrence of up t
## Abstrac -An lnvestgatlon of umqueness and muItipbclty of the steady states m an isothermal fliudlzed bed reactor and contmuous stured tank reactor IS presented Matenal balance equatums for the two phase model of DavIdson and Harnson and the moddied Partridge and Rowe model, are transformed mto