The present invention relates to a
fluidized bed reactor, which comprises a housing and a three-phase separation part, wherein the housing sequentially comprises an enlargement section, a transition section and a
straight tube section from top to bottom, the three-phase separation part is arranged inside the enlargement section and the transition section, and the side wall of the enlargement section is provided with a liquid
discharge port. The
fluidized bed reactor further comprises an inner
pipe and a gas-liquid distributer, wherein the inner
pipe is arranged inside the housing and extends from the lower portion of the
straight tube section to the lower portion of the enlargement section, the lower end opening of the inner
pipe is communicated with the
straight tube section, the upper end opening of the inner pipe is communicated with the enlargement section, the three-phase separation part is distributed around the upper portion of the inner pipe, and the gas-liquid distributer is arranged in the straight tube section and is positioned on the bottom of the inner pipe. According to the
fluidized bed reactor, material circulation can be driven completely through the
kinetic energy of the material on the inlet and the
density difference of the materials in different areas in the reactor, such that the whole process has the characteristic of energy saving; and the reactor utilization efficiency is high, such that the generation of the thermal
cracking reaction in the absence of the
hydrogen can be substantially reduced during the heavy oil hydrocracking process.