Hydrogenation of 2-methylindole using supported metal catalysts

Heidi Bernas; Narendra Kumar; Atte Aho; Reko Leino; Dmitry Murzin

doi:10.1016/j.catcom.2014.07.001

Hydrogenation of 2-methylindole using supported metal catalysts

Heidi Bernas, Narendra Kumar, Atte Aho, Reko Leino, Dmitry Murzin

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Sammanfattning

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.

Originalspråk	Odefinierat/okänt
Sidor (från-till)	41–44
Tidskrift	Catalysis Communications
Volym	56
DOI	https://doi.org/10.1016/j.catcom.2014.07.001
Status	Publicerad - 2014
MoE-publikationstyp	A1 Tidskriftsartikel-refererad

Åtkomst av dokument

10.1016/j.catcom.2014.07.001

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title = "Hydrogenation of 2-methylindole using supported metal catalysts",

abstract = "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.",

author = "Heidi Bernas and Narendra Kumar and Atte Aho and Reko Leino and Dmitry Murzin",

year = "2014",

doi = "10.1016/j.catcom.2014.07.001",

language = "Odefinierat/ok{\"a}nt",

volume = "56",

pages = "41–44",

journal = "Catalysis Communications",

issn = "1566-7367",

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TY - JOUR

T1 - Hydrogenation of 2-methylindole using supported metal catalysts

AU - Bernas, Heidi

AU - Kumar, Narendra

AU - Aho, Atte

AU - Leino, Reko

AU - Murzin, Dmitry

PY - 2014

Y1 - 2014

N2 - 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.

AB - 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.

U2 - 10.1016/j.catcom.2014.07.001

DO - 10.1016/j.catcom.2014.07.001

M3 - Artikel

SN - 1566-7367

VL - 56

SP - 41

EP - 44

JO - Catalysis Communications

JF - Catalysis Communications

ER -