Abstract
AbstractThe catalytic performance of a series of HY zeolites, modified by HF for olefin alkylation thiophenic sulfur (OATS) process, was evaluated. It was found that acid sites distribution could be controlled through the amount of HF. Under the optimized condition, activity, and selectivity of thiophene alkylation reaction in OATS could be greatly improved. At the same time, coking behavior was suppressed during the course. Copyright © 2008 Curtin University of Technology and John Wiley & Sons, Ltd.
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