CPC C10G 45/08 (2013.01) [C10G 1/002 (2013.01); C10G 1/10 (2013.01); C10G 65/02 (2013.01); C10G 69/02 (2013.01); C10G 2300/1003 (2013.01)] | 14 Claims |
1. A method for processing liquefied waste plastic (LWP), the method comprising the following steps:
a) providing an LWP stream containing diolefins and naphtha;
b) subjecting the LWP stream to a steam stripper to obtain a distillate containing diolefins and naphtha, and a distillate bottom;
c) subjecting the distillate to hydrotreatment reaction conditions in a presence of hydrogen and one or more hydrotreatment catalysts to produce diolefin depleted distillate, wherein the hydrotreatment reaction conditions include a temperature of 120-210° C., a pressure of 1-50 barg, and a liquid hourly space velocity (LHSV) of 1-5 h−1, and the one or more hydrotreatment catalysts are selected from CoMo and NiMo;
d) separating the diolefin depleted distillate to:
one or more fractions including:
at least a naphtha fraction with a boiling point below 180° C. at atmospheric pressure,
an optional middle fraction with a boiling point between 180° C. and 360° C. at atmospheric pressure; and
a bottom fraction; and
e) subjecting the naphtha fraction of step d) to hydroprocessing reaction conditions in a presence of hydrogen and one or more hydroprocessing catalysts to produce hydrogenated naphtha.
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