The invention relates to an inferior heavy oil
fluidization conversion technology. The inferior heavy oil
fluidization conversion technology comprises that
raw material oil is treated by a fractionating
tower, then enters into a lifting
pipe reactor, undergoes a
contact reaction with
coke carriers from a
coke carrier mixer, then enters into a first gas-
solid separation device and is separated; the separated reaction oil gas is fed into the fractionating
tower and is subjected to product division; the
coke carriers with coke is stripped and is divided into two parts, one of the two parts is fed into the coke carrier mixer, then is mixed with the high-temperature coke carriers from a
vaporizer and then is fed back to the lifting
pipe reactor, and other one of the two parts is fed into the
vaporizer, contacts with
oxygen-containing gas and
water vapor and undergoes a gasification reaction; the produced synthetic gas is separated by a second gas-
solid separation device, is fed into a follow-up section, and is subjected to heat
recovery and conversion; and the vaporized coke carriers are fed into the coke carrier mixer and is mixed with the coke carriers with the coke. Compared with the prior art, the inferior heavy oil
fluidization conversion technology has the advantages of simple process, low investment, strong
raw material adaptability, good
product distribution and good environmental benefits.