Hydrodesulfurization of condensate oil
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This post was last edited by hesonchang214 on 2018-8-30 at 22:17. I would like to ask the experts: the sulfur content in the condensate oil is 500 ppm, with mercaptans being the predominant form of sulfur. If a hydrodesulfurization process is used, what should be the operating pressure and temperature in the reactor to keep the sulfur content below 10 ppm for fractions with a boiling point below 220°C?
This post was last edited by kunn163 on 2016-10-27 09:22. Please give me some advice, experts! ! ! Are there any other requirements? I haven’t been involved in hydrogenation processes either, so please forgive me! If the operating pressure is 0.5 MPa and the operating temperature is 350°C, is it generally feasible?
Bro, I’m just getting started. . I have a question. Understand the process – how to proceed? Under normal circumstances, what should the operating parameters be?
I have previously processed Hainan condensate oil. Control the boiling range at 220... followed by alkali washing, water washing, sand filtration, and carbon adsorption. . . . Reducible thiol