id	author	title	date	pages	extension	mime	words	sentence	flesch	summary	cache	txt
cet-6577		cet-6577		6	.pdf	application/pdf	3034	83	41	Table 1: Composition of products of rape oil conversion under optimal conditions Rape oil conversion products Product composition, wt % 360°C , 1.2 h–1 420°C, 2.4 h–1 С1 0.54 1.04 С2 4.89 4.83 C2= 0.18 0.32 C3 11.71 10.79 C3= 0.37 0.75 iso-C4 9.50 5.88 n-С4 5.30 2.19 C4= 1.49 1.81 iso-С5 9.91 4.52 n-C5 2.60 1.46 С5= 0.66 1.12 2,3-Me-C4 1.09 0.45 iso-C6 2.04 0.94 n-C6 3.40 0.72 Benzene 7.04 6.56 Toluene 16.92 18.42 Ethylbenzene 3.79 4.81 o,p-Xylene 9.24 13.06 m-Xylene 2.23 3.15 Propylbenzene 0.00 0.94 Methylethylbenzene 4.16 5.93 1,2,3-Trimethylbenzene 0.80 1.40 Methylphenylethylene 0.61 1.01 1,2-Diethylbenzene 0.00 1.61 α-Phenyl-β-ethylethylene 0.00 0.96 Naphthalene 0.00 1.16 α-Methylnaphthalene 0.63 1.40 СО 0.58 2.55 СО2 0.33 0.21 Σ 100.00 100.00 Application of Pt/Al2O3 allows to improve the efficiency of rape oil conversion towards valuable hydrocarbons in comparison with Ni containing catalysts described by Mikulec J. et al., 2009 and Kovács S. et al., 2010 due to realization of process in one step and also reducing the loss of valuable carbon mass via glycerol and acyl fragments condensation.	cache/cet-6577.pdf	txt/cet-6577.txt