Catalytic cracking unit-hydrogenation unit combined energy-saving technological process
A technology for a catalytic cracking unit and a process flow is applied in the field of the combined energy-saving process flow of a catalytic cracking unit and a hydrogenation unit, which can solve the problems of large processing capacity and complex flow of the main fractionation tower, and achieves an increase in the overhead circulation of the main fractionation tower of the catalytic cracking unit. Effect of heat output, reduction of cooling load and rich gas compression load, and reduction of throughput
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[0031] In this embodiment, a combined energy-saving technological process of catalytic cracking unit and hydrogenation unit, the following improvements are made on the original catalytic cracking unit and technological process:
[0032] The rich diesel oil at the bottom of the reabsorption tower is re-refined from the main fractionating tower and directly fed to the raw material buffer tank of the catalytic diesel hydrocracking unit, and the heat exchanger 11 of the original lean diesel oil to rich diesel oil is canceled, and other pipeline processes remain unchanged.
[0033] Its process flow chart is as figure 2 As shown, the specific process flow is as follows:
[0034] The reaction oil and gas from the reaction unit enters the lower part of the herringbone baffle of the main fractionation tower 1, contacts with the 275°C circulating oil slurry flowing down from the top of the herringbone baffle from bottom to top, and enters the fractionation part after being washed and d...
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