Light gasoline was produced from kerosene at industrial vapor phase hydrocracking plants. The system analysis of the plants was made from the engineering point of view.
Here, the calculation model of gasoline yield per weight was proposed, and it was clarified that according to the increase of LHSV-1, the yield increased following the equation of the 1st order reac-tion rate.
The longitudinal reactor temperature was measured and increased monotonously towards the outlet of the reactor from the inlet. The temperature rising with reaction was 66-88k according to operating conditions. Thus the hot spot trouble was not observed.
