Participants
| Role | Name | HCID | Charge |
|---|
| Reactant | Isobutanol | HCID 6560 | — |
| Reactant | Isobutylene | HCID 8255 | — |
| Product | Isopropyl tert-butyl ether | HCID 118384 | — |
Reaction Steps
In the etherification stage, isobutene is reacted with alcohols, preferably with isobutanol, over an acid catalyst, preferably an acid ion exchanger, to form ethers, preferably isobutyl tert-butyl ether. In one embodiment of the invention, the reaction is carried out in a three-stage reactor cascade in which the reaction mixture flows from the top downward through flooded fixed-bed catalysts. In the first reactor, the inlet temperature is from 0 to 60° C., preferably from 10 to 50° C.; the outlet temperature is from 25 to 85° C., preferably from 35 to 75° C., and the pressure is from 2 to 50 bar, preferably from 3 to 20 bar. At a ratio of isobutanol to isobutene of from 0.8 to 2.0, preferably from 1.0 to 1.5, the conversion is from 70 to 90%.
Provenance & Evidence
| DOI | 10.6084/m9.figshare.5104873.v1 |
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| Patent number | US06580009B2 |
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| Source dataset | uspto-grants-2003_06 |
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| ORD ID | ord-ee1968a4091c46cea07b1187e240fe4a |
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| Source note | uspto-grants-2003_06 |
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