A
residual oil conversion process method and a
reaction system belong to the field of oil refining
processing, and the process method comprises the following steps: mixing a heavy inferior
residual oil raw material with a dispersed
molybdenum-containing catalyst and a partially circulated heavy fraction
cracking product; after heat exchange and temperature rise, pretreatment is conducted through a 10-30 KHz
ultrasonic device; after preheating, entering a
slurry bed hydrogenation reactor, and carrying out a hydro-
conversion reaction in a
hydrogen atmosphere under the conditions of 380-500 DEG C and 5-18 MPa; after subsequent processes and equipment separation, the heavy liquid
hydrocarbon part enters a catalytic
cracking device and is subjected to a
contact reaction with a
residual oil cracking catalyst containing aluminum extraction and
silicon supplement Y
zeolite under the conditions that the temperature is 500-540 DEG C and the catalyst-oil ratio is 5-15; fractionating the product in a fractionating
tower; the
reaction system comprises an ultrasonic pretreatment device, a
slurry bed reactor, a catalytic cracking device, a product fractionating
tower and heat exchange, separation and circulation equipment. According to the method, the conversion efficiency and process stability of the heavy inferior residual oil
raw material are improved, the yield of light fraction
gasoline is increased, the
energy consumption is reduced, and the method has good economical efficiency and practicability.