Participants
| Role | Name | HCID | Charge |
|---|
| Reactant | Benzene | HCID 241 | — |
| Reactant | Propane | HCID 6334 | — |
| Reactant | Propylene | HCID 8252 | — |
| Product | Cumene | HCID 7406 | — |
Reaction Steps
The first reactor effluent stream enters a heat exchanger 44. In the heat exchanger 44, the first reactor effluent stream exchanges heat indirectly with a flashed depropanizer bottoms stream from a line 42. The cooled first reactor effluent stream passes through a line 26 and is admixed with a mixture of propane and propylene that enters the process in a line 22. This produces an alkylation zone feed stream carried by a line 28. This stream may be heated in a heat exchanger or a heater, which is not shown, and enters a second reactor 30. The feed stream contacts a zeolite catalyst maintained at alkylation-promoting conditions to effect the reaction of at least a major portion of the propylene with benzene to form cumene. A second reactor effluent stream comprising benzene, cumene, and poly-alkylated hydrocarbons exits the second reactor 30 in a line
Provenance & Evidence
| DOI | 10.6084/m9.figshare.5104873.v1 |
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| Patent number | US05336821 |
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| Source dataset | uspto-grants-1994_08 |
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| ORD ID | ord-f22ba0e63ad84f5cb96bd861d4d294a3 |
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| Source note | uspto-grants-1994_08 |
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