Abstract
1. Single-stage hydrodearomatization of kerosine cuts at pressures up to 50 kgf/cm2 has been studied with a view to the production of high-quality jet fuels. 2. It has been shown that hydrodearomatization of low-sulfur feedstocks (below 0.03% sulfur) on AP-64 reforming catalyst can give a 30–35% relative reduction in the content of aromatic hydrocarbons. 3. A special sulfur-resistant catalyst of the GR type has been developed for the single-stage process; with this catalyst, a relative reduction of 70–75% in the content of aromatic hydrocarbons can be achieved with a feedstock sulfur content of 0.4% by weight.
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