Material state in the diesel hydrogenation reactor
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In a diesel hydrogenation trickle-bed reactor, what is the vaporization rate of the diesel liquid phase at a reaction temperature of 360 degrees Celsius and a pressure of 3–4 MPa? According to the book \"Hydroprocessing Processes and Engineering\" written by Academician Li Dadong, it is recommended that the gasification rate at the reactor inlet be 1. Is this the case in actual industrial operations? Also, does the diesel hydrogenation reaction take place in the gas phase or in the liquid phase? I hope the veterans on this forum will be kind enough to offer their guidance!
Liquid-phase hydrogenation is in the liquid phase, while gas-phase hydrogenation is in the gas phase.
Diesel reactors should be designed in two types, right: gas phase and gas-liquid two-phase
But at this point, can’t the phase state of the materials be determined based on the operating conditions? That is, at 6 MPa and 340 degrees Celsius, diesel is in a trickle bed state
But at this point, can’t the phase state of the materials be determined based on the operating conditions? That is, at 6 MPa and 340 degrees Celsius, diesel is in a trickle bed state