Combined process of hydrotreating and catalytic cracking for inferior oil products
A technology of hydrotreating and catalytic cracking, which is applied in the fields of hydrotreating process, petroleum industry, and hydrocarbon oil treatment, etc. It can solve the problem of products that cannot meet the requirements of production performance, limited increase in cetane number, and cannot well meet high Quality Vehicle diesel product quality index requirements and other issues
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Embodiment 1
[0044] This embodiment adopts the combined process of hydrotreating and catalytic cracking of inferior oil products provided by the present invention. After mixing the raw oil and hydrogen, it enters the hydrotreating zone and contacts with the hydrogenation protection catalyst, hydrodemetallization catalyst and hydrodesulfurization catalyst in sequence. The hydrogenation reaction is carried out, and the effluent from the hydrogenation reaction zone enters the hot high-pressure separator for gas-liquid separation after heat exchange, and the hot high-separation oil and hot high-separation gas are separated, and the hot high-separation gas enters the cold storage after heat exchange and cooling. High-pressure separator, after separation, cold high-fraction gas and cold high-fraction oil are obtained. After the cold high-fraction gas is dehydrogenated, it enters the circulating compressor to increase the pressure and then circulates to the hydrogenation reactor inlet. The new hydr...
Embodiment 2
[0061] This embodiment adopts the combined process of residual oil hydrotreating and catalytic cracking provided by the present invention, and the gradation of raw materials and catalysts in the hydrogenation reaction is consistent with that of Embodiment 1.
[0062] This embodiment adopts the combined process of hydrotreating and catalytic cracking of inferior oil products provided by the present invention. After mixing the raw oil and hydrogen, it enters the hydrotreating zone and contacts with the hydrogenation protection catalyst, hydrodemetallization catalyst and hydrodesulfurization catalyst in sequence. The hydrogenation reaction is carried out, and the effluent from the hydrogenation reaction zone enters the hot high-pressure separator for gas-liquid separation after heat exchange, and the thermal high-separation oil and hot high-separation gas are separated, and the hot high-separation gas enters after heat exchange and cooling. Cold high-pressure separator, after sepa...
Embodiment 3
[0064] This embodiment adopts the combined process of residual oil hydrotreating and catalytic cracking provided by the present invention, and the gradation of raw materials and catalysts in the hydrogenation reaction is consistent with that of Embodiment 1.
[0065]This example adopts the combination process of residual oil hydrotreating and catalytic cracking provided by the present invention. This example adopts the combined process of hydrotreating and catalytic cracking of inferior oil products provided by the present invention. The raw oil and hydrogen are mixed and then enter the hydrotreating zone. Contact with hydrogenation protection catalyst, hydrodemetallization catalyst and hydrodesulfurization catalyst in sequence to carry out hydrogenation reaction. After heat exchange, the effluent from the hydrogenation reaction zone enters the hot high-pressure separator for gas-liquid separation, and the separation obtains hot high-fraction oil and Hot high-separation gas, th...
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