Abstract
The present invention relates to a method for continuous production of 2,3-butanediol by hydrogenation of 3-hydroxybutanone with hydrogen in the presence of a heterogeneous hydrogenation catalyst filled in one or more fixed-bed flow tubular reactor systems comprising one or more tubes with an inner diameter from 1 mm to 6 mm.
| Original language | English |
|---|---|
| Patent number | EP3483138 (A1) |
| IPC | C07C29/145||C07C31/20 |
| Priority date | 9/11/17 |
| Publication status | Published - 9 Nov 2017 |
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