Derivation and Application of a Steady Stale Mathematical Model of an Isopropanol-Acetne Reactor
As a part of the study of the computer control and optimisation of a pilot scale plant, a mathematical model is derived for the steady-state of the process in which acetone and methyl-isobutyl ketone are made from isopropanol by heterogeneous catalysis in a tubular reactor. Using the model as an ana...
| Main Authors: | , , , |
|---|---|
| Format: | Article |
| Language: | English |
| Published: |
SAGE Publishing
1969-11-01
|
| Series: | Measurement + Control |
| Online Access: | https://doi.org/10.1177/002029406900201103 |