Participants
| Role | Name | HCID | Charge |
|---|
| Reactant | Oxygen | HCID 977 | — |
| Reactant | Cumene | HCID 7406 | — |
| Reactant | 1-Ethyl-4-Methylbenzene | HCID 12160 | — |
| Product | Alpha-Methylstyrene | HCID 7407 | — |
Reaction Steps
This example illustrates the dehydrogenation of cumene and p-ethyltoluene using a diluent comprising steam and nitrogen. Three and three-tenths of the catalyst prepared in Example I, ground to 18 to 40 mesh, was employed in the reactor described in Example I. Initially p-ethyltoluene was flowed into the reactor at 0.38 liquid hourly space velocity, 11:1 diluent to p-ethyltoluene ratio (8:1 steam and 3:1 nitrogen) at 588° C. yielding a relatively poor conversion and selectivity. The catalyst was decoked with 5% oxygen and nitrogen for about 1 hr. Cumene was then run at 0.38 liquid hourly space velocity, 11:1 diluent ratio (8:1 steam and 3:1 nitrogen) at 588° C. providing 40% conversion to alphamethylstyrene and 88% selectivity. The feed was then switched from cumene to p-ethyltoluene using the same diluent dilution and conditions providing 22% conversion to p-methylstyrene and 93% selectivity. Conditions were then changed to 0.72 liquid hourly space velocity, 10:1 diluent ratio for the p-ethyltoluene (8:1 steam and 2:1 nitrogen) at 598° C. yielding 40% conversion and 92% selectivity to p-methylstyrene.
Provenance & Evidence
| DOI | 10.6084/m9.figshare.5104873.v1 |
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| Patent number | US04590324 |
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| Source dataset | uspto-grants-1986_05 |
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| ORD ID | ord-496553a6097c46dfa569c07b96b29155 |
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| Source note | uspto-grants-1986_05 |
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