Abstract
1. Hydrorefining of the 130–215‡ aviation kerosene fraction into which 3% naphthalene by wt. has been introduced over aluminum-cobalt-molybdenum catalyst has been studied. 2. It has been shown that at 275–300 ‡C the degree of naphthalene hydrogenation is 85-75%; thereupon the desulfurization of the raw material takes place to the extent of 69–84%.
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