Аннотации:
© 2019 Published under licence by IOP Publishing Ltd. A fluidized bed reactor designed for the dehydrogenation of isobutane is considered. The process takes place at high temperature and with heat absorption. A feature of the apparatus is the mechanism of block heating due to the catalyst entering through the pipe located in the center. The analysis of the effect of the grids located in the apparatus on the reactor heating is carried out.