Method for producing low-carbon olefins
A low-carbon olefin and metal technology, which is applied in the production of bulk chemicals, hydrocarbon oil treatment, hydrocarbon cracking and hydrocarbon production, etc., to achieve the effects of reducing viscosity, large-scale industrial promotion value, and avoiding complicated processes
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Embodiment 1
[0043] Using waste lubricating oil provided by a refinery as raw material, the raw material oil is passed through a vacuum distillation device to obtain light and heavy distillate oils. Among them, the distillation temperature of 90% of the light distillate oil is controlled at 450°C. The total metal or IIB metal content is 0ppm, and the VIIIB metal total content is 5ppm. The light distillate oil in the light fraction is preheated to 320°C by a heating furnace, enters the riser reactor for reaction, contacts with the high-temperature catalyst of the regenerator, and then vaporizes The reaction is carried out under the following conditions: the reaction temperature is 560°C, the weight ratio of the catalyst to the pretreated material (hereinafter referred to as the agent-oil ratio) is 10:1, and the weight ratio of water vapor to the pretreated material (hereinafter referred to as the water-oil ratio) ) is 0.1:1, and the pressure is 200kPa. The generated oil and gas are separated...
Embodiment 1-1
[0045] The same raw materials and devices as in Example 1 are used, except that the oil gas generated by coking does not enter the riser reactor, but enters the fractionation device, separates gas, gasoline, diesel oil and wax oil, and exits the device. The product distribution is shown in Table 3.
Embodiment 1-2
[0047] The same raw materials and devices as in Example 1 are used, except that the coker oil gas is first separated from the gas phase by a fractionation tower, and the liquid is returned to the riser reactor to continue the reaction. The product distribution is shown in Table 3.
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