HuagongsheHuagongshe Chemistry Print Report · For research reference only
Benzene → Cumene
Participants
| Role | Name | HCID | Charge |
|---|---|---|---|
| Reactant | Benzene | HCID 241 | — |
| Reactant | Propylene | HCID 8252 | — |
| Product | Cumene | HCID 7406 | — |
Reaction Steps
The experimental setup of Example 1 is employed in the alkylation of benzene with propylene to form cumene, with the exception of the following changes. The pretreatment bed containes 20 g mordenite catalyst instead of 10 g. Benzene flow over the guard bed is 40 hr−1. Benzene flow over the alkylation catalyst is 800 hr−1. Propylene flow into the alkylation reactor is 12 hr−1. Combined propylene and benzene flow through the alkylation reactor is 812 hr−1. Benzene/propylene molar ratio is 66.7. Both the pretreatment zone and alkylation zone are started at 150° C. FIG. 2 shows the effect of varying the temperatures of the pretreatment zone and the alkylation reactor on the yield of cumene.
Provenance & Evidence
| DOI | 10.6084/m9.figshare.5104873.v1 |
|---|---|
| Patent number | US06297417B1 |
| Source dataset | uspto-grants-2001_10 |
| ORD ID | ord-8aa08926300649e0aa23972a01b10fbb |
| Source note | uspto-grants-2001_10 |