Research Article
Design and Control of Glycerol-tert-Butyl Alcohol Etherification Process
Table 2
Boiling point for pure components and azeotropes at
bar.
| Component/azeotrope | T/(°C) | Destination |
| IB | −6.25 | Byproduct | TBA (0.6209)/W (0.3791) | 79.97 | — | TBA | 82.42 | Recycle | W | 100 | Byproduct | G (0.1951)/DE (0.8049) | 233.5 | — | DE | 240.4 | Product | ME | 256.61 | Recycle | G | 287.85 | Recycle |
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