Abstrakti
The hydrogenation of 2-methylindole to 2-methylindoline in toluene was studied at 60 degrees C and 40 bar hydrogen pressure in a batch mode using a range of carbon, alumina, and zeolite supported metal catalysts were performed in toluene. The results were compared with a more conventional catalytic system containing besides 5% Pt/C also 1.2 eq. of p-toluenesulfonic add in ethanol:water (50:50 v/v). The highest turnover frequency (TOF) was obtained a zeolite supported iridium catalyst.
Alkuperäiskieli | Ei tiedossa |
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Sivut | 41–44 |
Julkaisu | Catalysis Communications |
Vuosikerta | 56 |
DOI - pysyväislinkit | |
Tila | Julkaistu - 2014 |
OKM-julkaisutyyppi | A1 Julkaistu artikkeli, soviteltu |