In recent years, in order to reduce the procurement cost of raw materials, the trend of inferior quality and heavy quality of raw materials has intensified, characterized by the density of wax oil, slag oil, residual carbon value, metal content increased year by year, heavy fractions, low saturated hydrocarbon content, high heavy metal content, poor cracking performance. Although raising the reaction temperature can increase the reaction depth, but also make the reaction trend of non-selective secondary cracking and thermal cracking significant, resulting in a decrease in light oil yield, increased dry gas and coke yield, poor catalyst regeneration effect, poor anti-pollution performance, reaction, fractionation system coking serious, energy consumption and catalyst consumption increased, increased costs. At the same time, the caramel temperature of the regenerator has been at the upper limit of the process index, the separation effect of the cyclone separator is not ideal, and the catalyst consumption remains high.
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