The necessity of jacketed heating for the process pipeline from the catcher to the hydrogenation reactor inlet.
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This post was last edited by liaifeng on 2018-9-10 at 18:54. In the design, the process pipeline from the catcher to the inlet of the hydrogenation reactor is equipped with jacket heating. Considering the possibility of leaks in this jacket heating system, as well as the difficulties in installation and associated costs, is it really necessary to use jacket heating? Can the goal also be achieved using 1.0 MPa steam with triple insulation?
How long is your pipeline from the collector to the exhaust gas heater?
The design is not finalized yet; I have some questions and would like to know more!
The pipeline from the catcher to the hydrogenation reactor does not require a jacket, as the process gas flows continuously and no condensation occurs.