Naphtha hydroprocessing with mercaptan removal
a technology of mercaptan removal and hydroprocessing, which is applied in the field of hydroprocessing of naphtha with removal of mercaptan from product, can solve the problems of increased production costs of high octane fuels, loss of desirable molecules contributing to desirable octane, and further loss of desirable molecules contributing to high octan
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[0021] The feedstocks used in the present process comprise petroleum fractions boiling in the gasoline boiling range. Such feeds include fluid catalytically cracked (FCC) naphthas, steam cracked naphthas and coker naphthas boiling from about 65° F. to 480° F. (18° C. to 221° C.) as determined by ASTM D-86. Such naphthas include light cracked naphthas, intermediate cracked naphthas, heavy cracked naphthas and full range naphthas. Naphthas typically contain paraffins, olefins, naphthenes and aromatics as well as heteroatom species containing nitrogen and sulfur. Olefin contents of naphthas can range up to 60 wt. %, based on naphtha with typical olefin contents in the range from 5 to 40 wt. %. Sulfur contents of naphthas may range from 50 to greater than 5000 ppmw, based on naphtha. Nitrogen contents for these feeds are typically less than 500 ppmw. Olefin, nitrogen and sulfur contents may be determined by standard analytical techniques.
[0022] With regard to olefin and sulfur contents...
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