Reaktionsgleichung
[CH:1]([CH2:3][CH2:4][CH2:5][CH2:6][C:7]([O:9][CH3:10])=[O:8])=[O:2].[NH3:11].[H][H]>>[NH2:11][CH2:1][CH2:3][CH2:4][CH2:5][CH2:6][C:7]([O:9][CH3:10])=[O:8].[C:1]1(=[O:2])[NH:11][CH2:7][CH2:6][CH2:5][CH2:4][CH2:3]1Komponenten
5
Versuchsvorschrift
Thereafter, 198.5 g/hour of a 10.0% strength methanolic methyl 5-formylvalerate solution and 46.4 g/hour of liquid ammonia were pumped through the reactor from below, while simultaneously passing through hydrogen, at 80° C. and under 100 bar. The reaction mixture passed from the top of the reactor via a condenser into a separator, from which 243 g/hour of product mixture and 22.6 l/hour of waste gas were removed. According to quantitative gas chromatographic analysis, the reacted mixture contained 7.22% of methyl 6-aminocaproate and 0.15% of caprolactam, corresponding to yields of 87.8% of methyl 6-aminocaproate and 2.4% of caprolactam, percentages being based on the completely converted methyl 5-formylvalerate.
Aufarbeitung
- customThe reaction mixture passed from the top of the reactor via a condenser into a separator, from which 243 g/hour of product mixture and 22.6 l/hour of waste gas
- customwere removed
Quellen und Nachweise
- ORD-Eintrag
- ord-d2d745ff033843be8fedabce2b38302f
- Quelldatensatz
- uspto-grants-1988_08
- Patentnummer
- US04766237
Verknüpfte Notizen
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