Abstract
Selective hydrocracking is most often used to improve the antiknock properties of reformates, raffinates remaining after extraction of aromatic hydrocarbons from aromatic naphthas, and isomerizates [i]. In a number of cases, however, this process may be applied to raise the octane number of straight-run naphtha cuts. Here, the sulfur resistance of the selective hydrocracking catalysts may become the decisive factor in selecting the processing scheme for these cuts.
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