Continuous modification and visbreaking process for crude oil
A crude oil and upgrading technology, which is applied in the petroleum industry, hydroprocessing process, and hydrocarbon oil treatment, can solve the problems of time difference advantage annihilation, etc., and achieve the effect of adjustable cracking depth, wide range of sources, and better product properties and distribution
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Embodiment 1
[0046] With Venezuelan super heavy oil as raw material and supercritical benzene as solvent, Venezuelan super heavy oil takes 400°C as the cut point, and is cut into two stages of <400°C distillate oil and 400°C+residue through distillation tower A. 400°C + residual oil is preheated by heating furnace B, mixed with benzene preheated by heating furnace A at a ratio of 1:3 (wt%) to obtain the target reaction temperature, and then the mixture enters an upflow vis-reducing reactor with a reaction pressure of 10MPa , the reaction temperature is 400°C, and the reaction residence time is 5 minutes. After the reaction, leave the visbreaking reactor from the top of the reactor, the visbreaking product enters the flash tower, and the solvent separated from the top of the tower is recycled back to the visbreaking reactor, and the bottom oil of the flash tower enters the distillation tower B, which is cut into IBP-180 The light distillate at the top of the tower, the side stream at 180-39...
Embodiment 2
[0067] Using Canadian oil sand bitumen as raw material and supercritical toluene as solvent, the oil sand bitumen takes 350°C as the cut point, and passes through distillation tower A to cut distillate oil <350°C and 350°C+residue. 350℃+residual oil is preheated by the heating furnace, and mixed with the preheated benzene solvent in a certain proportion, and the temperature after mixing can reach the reaction temperature. The mixture then enters an upflow vis-reducing reactor with a reaction pressure of 10 MPa, a reaction temperature of 410° C., and a reaction residence time of 3 minutes. After the reaction, the visbroken product leaves the visbroken reactor from the top of the reactor, and after heat exchange, the visbroken product is lowered to a suitable temperature and enters the flash tower. The product enters the distillation tower B, which is cut into IBP-200°C distillation tower B overhead distillate, 200-350°C side cut and 350°C+distillation tower B viscosity-reduced ...
Embodiment 3
[0091] Chadian crude oil is used as raw material, and Chadian crude oil is paraffinic base crude oil. Using supercritical benzene as the solvent and 540°C as the cut point, after distillation A, it is cut into distillation tower A distillate oil and distillation tower A residue oil. After the 540℃+ vacuum residue is preheated by the heating furnace, it is mixed with heated benzene in a certain proportion, and the temperature after mixing can reach the reaction temperature. The mixture then enters an upflow vis-reducing reactor for vis-reducing reaction, with a reaction pressure of 10 MPa, a reaction temperature of 360° C., and a reaction residence time of 5 minutes. After the reaction, the visbroken product leaves the visbroken reactor from the top of the reactor and enters the flash tower, and the benzene separated from the top of the tower is recycled back to the visbroken reactor, and the product obtained at the bottom of the flash tower enters the distillation tower B and ...
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