The following data for the hydrogenation of i-octene to form i-octane were obtained using a differential reactor operated at 200ºC.
|
| Partial Pressure (atm) | ||
Run | Rate (mol/g.h) | Hydrogen | i-Octene | i-Octane |
1 | 0.0362 | 1 | 1 | 0 |
2 | 0.0239 | 1 | 1 | 1 |
3 | 0.0390 | 3 | 1 | 1 |
4 | 0.0351 | 1 | 3 | 1 |
5 | 0.0114 | 1 | 1 | 3 |
6 | 0.0534 | 10 | 1 | 0 |
7 | 0.0280 | 1 | 10 | 0 |
8 | 0.0033 | 1 | 1 | 10 |
9 | 0.0380 | 2 | 2 | 2 |
10 | 0.0090 | 1 | 1 | 4 |
11 | 0.0127 | 0.6 | 0.6 | 0.6 |
12 | 0.0566 | 5 | 5 | 5 |
(a) Develop a rate law, and evaluate all the rate law parameters.
(b) Suggest a mechanism consistent with the experimental data Hydrogen and i-octene are to be fed in stoichiometric proportions at a total rate of 5 mol/min at 200ºC and 3 atm.
(c) Neglecting pressure drop, calculate the catalyst weight necessary to achieve 80% conversion of i-octene in a CSTR and in a plug-flow reactor.
(d) If pressure drop is taken into account and the -in. catalyst pellets are packed in -in. schedule 80 pipes 35 ft long, what catalyst weight is necessary to achieve 80% conversion? The void fraction is 40% and the density of the catalyst is 2.6 g/cm3
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