Heavy, residual oil hydrogenating catalyst and its preparation
A desulfurization catalyst and residual oil hydrogenation technology, which is applied in refining to remove heteroatoms, etc., can solve the problems of not fully exerting the promotion effect of TiO2, catalyst pore volume, specific surface reduction, catalyst performance impact, etc., to avoid competitive adsorption, Reduce the loss of pore volume and specific surface, the effect of high pore volume and specific surface
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Embodiment 1
[0022] The concentration is 30g Al 2 o 3 500mL of sodium metaaluminate solution per liter is placed in the ultrasonic transducer, the ultrasonic transducer is controlled to transmit power to 200W, the frequency is 25kHz, the temperature is 25°C, and carbon dioxide gas with a concentration of 40v% is introduced into it, and it is added under constant stirring. The concentration of slurry is 20g TiO 2 / l metatitanic acid slurry (pH value is 8.0, particle size is less than 40μm), so that the carrier contains TiO 2 It is 10% by weight, and the carbon dioxide gas is continuously fed until the pH value of the slurry is 10, the carbon dioxide gas is stopped, the slurry is aged for 1.0 hour, and the ultrasonic transducer is turned off. Then filter and wash with deionized water until the carrier contains Na + When it is less than 0.05w% by weight, dry (120° C.) for 4 hours, and then crush to 180 mesh to obtain titanium-containing aluminum hydroxide A.
Embodiment 2
[0024] Compared with Example 1, the transmission power of the ultrasonic transducer is changed to 50W and the frequency is 80kHz, and the amount of other materials and operating conditions are the same as in Example 1, and titanium-containing aluminum hydroxide B is obtained.
Embodiment 3
[0026] Compared with Example 1, the transmission power of the ultrasonic transducer is changed to 800W and the frequency is 50kHz, and the amount of other materials and operating conditions are the same as in Example 1, and titanium-containing aluminum hydroxide C is obtained.
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