A method and system for upgrading inferior oil with high yield of heavy upgraded oil
A low-quality oil upgrading technology, which is applied in the treatment of hydrocarbon oil, petroleum industry, hydrotreating process, etc., to achieve the effect of improving the effective utilization of resources, improving economic efficiency, and high upgrading efficiency
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specific Embodiment approach
[0076] A specific embodiment, in step (3), the separation treatment includes step (3-1) and step (3-2):
[0077] (3-1) The obtained conversion product in the step (2) is separated at the second pressure and the second temperature to obtain a gas component and a liquid component; in the step (3-1), gas products such as hydrogen are preferably separated, The gas component is rich in hydrogen, preferably the hydrogen content is above 85% by weight; the second pressure can be 10-25 MPa, preferably 13-20 MPa, for the convenience of measurement, the second pressure generally refers to the separation of gas components The outlet pressure when the separation device is opened, the second temperature can be 380-470 ° C, preferably 400-440 ° C, for the convenience of measurement, the second temperature generally refers to the outlet temperature when the liquid component leaves the separation device; in this step, the separation The method can be distillation, fractional distillation and ...
Embodiment 1-5
[0100] In a medium-sized device, the inferior oil as the raw material for upgrading is firstly extracted and separated, the obtained residue is mixed with the catalytic cracking oil slurry and entered into a slurry bed reactor for conversion reaction, and the conversion product is subjected to separation treatment, and the separation treatment is carried out in two fractionation towers. The first separation product and the second separation product are obtained, the first separation product is mixed with the upgraded raw material and enters the extraction separation unit, and the obtained residue is partially thrown out, and part is mixed with the catalytic cracking oil slurry to continue the conversion reaction, conversion reaction and separation. The specific conditions and results of the treatment are listed in Table 2-1, Table 2-2 and Table 2-3.
[0101] As can be seen from Tables 2-2 and 2-3, by adopting the method and system of the present invention, the conversion rate o...
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