HYDROTREATING COKER KEROSENE WITH A SEPARATE TRIM REACTOR
摘要
<p>A process for hydrotreating coker kerosene is described. Instead of a post treat reactor, a smaller trim reactor zone which operates at a lower pressure than the post treat reactor is used downstream of the product stripper. The trim reactor uses a noble metal catalyst to reduce the BI of the stripped product to less than 150, and desirably in the range of 50 to 100.</p>
