Participants
| Role | Name | HCID | Charge |
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| 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 acidic catalyst, preferably over an acidic ion exchanger, to give ethers preferably isobutyl tert-butyl ether. According to one embodiment of the invention, the reaction is carried out in a three-stage reactor cascade, in which the reaction mixture flows through flooded fixed-bed catalysts from top to bottom. In the first reactor the inlet temperature is 0 to 60° C., preferably 10 to 50° C.; the outlet temperature is between 25 and 85° C., preferably between 35 and 75° C., and the pressure is 2 to 50 bar, preferably 3 to 20 bar. At a ratio of isobutanol to isobutene of from 0.8 to 2.0, preferably 1.0 to 1.5, the conversion is between 70 and 90%.
Provenance & Evidence
| DOI | 10.6084/m9.figshare.5104873.v1 |
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| Patent number | US07566799B2 |
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| Source dataset | uspto-grants-2009_07 |
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| ORD ID | ord-8b6fc49970d340e4a4c5042269bf1b1d |
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| Source note | uspto-grants-2009_07 |
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