Suspension bed hydrogenation process for processing heavy oil
A suspended bed, heavy oil technology, applied in hydrotreating process, treatment of hydrocarbon oil, petroleum industry, etc., can solve the problems of uneven mixing, insufficient reaction, unsatisfactory hydrogenation product separation effect, etc., and achieve good hydrogenation catalysis. Activity, the effect of improving conversion rate and light oil yield
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Embodiment 1
[0076] Such as figure 1 As shown, the suspended bed hydrogenation process for heavy oil provided in this embodiment includes the following steps:
[0077] (1) select residual oil as the raw material oil of this process, get half of the residual oil and mix it with the suspension bed hydrocracking catalyst to form a mixture, and carry out primary shear and secondary shear to the mixture successively, Obtain catalyst slurry;
[0078] (2) Mix the catalyst slurry with the remaining residual oil and hydrogen and send it into the suspension bed hydrogenation reactor, and control the operating pressure in the suspension bed hydrogenation reactor to 18MPa, the temperature to 425°C, and the volume of hydrogen oil The ratio is 1000 for hydrocracking reaction;
[0079] (3) After step (2) reacted for 1.5h, the obtained suspension bed hydrogenation product was subjected to thermal high-pressure separation at 18MPa and 400°C, and hot high-separation gas and hot high-separation oil were co...
Embodiment 2
[0084] Such as figure 1 As shown, the suspended bed hydrogenation process for heavy oil provided in this embodiment includes the following steps:
[0085] (1) Purification treatment of coal tar
[0086] Air is introduced into the coal tar so that the particle size is 0.2mm and the specific surface area is 50m 2 / g of kaolin powder and coal tar are back-mixed and contacted at a mass ratio of 0.1:1 and adsorbed at 50°C and 0.5MPa. The air flow required for each 1kg of kaolin powder is 0.5m 3 / s; After the adsorption is completed, settle and stratify, collect the upper layer material, and then perform solid-liquid separation on the upper layer material, and the collected liquid phase is the purified coal tar;
[0087] Compared with the coal tar before the purification treatment, the residual carbon value in the coal tar after the purification of this embodiment is reduced to 0.1%, which is reduced by 79%; the content of asphaltene is reduced by 76%; the colloid is reduced by 80...
Embodiment 3
[0095] Such as figure 1 As shown, the suspended bed hydrogenation process for heavy oil provided in this embodiment includes the following steps:
[0096] (1) Preparation of catalyst slurry
[0097] Select coal tar as the raw material oil of this process, please refer to Figure 5 Take half the amount of coal tar and inject it into the solvent buffer tank 51, after being buffered by the solvent buffer tank 51 and pressurized by the solvent booster pump 58, it enters the Venturi tube 56, and at the same time, the suspended bed hydrocracking catalyst enters from the solid catalyst The material system 55 also enters into the Venturi tube 56, and the coal tar and the catalyst are initially mixed in the Venturi tube 56 and then enter the slurry preparation tank 52, and form a primary slurry under the agitation of the stirring device 54, which is prepared in the tank. The temperature is 90°C, and the pressure in the preparation tank is normal; then the first-stage slurry is sheare...
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