A kind of inferior heavy oil hydrogenation desulfurization catalyst and preparation method thereof
A technology for hydrodesulfurization and low-quality heavy oil, applied in catalyst activation/preparation, chemical instruments and methods, physical/chemical process catalysts, etc., can solve the problems of reduced carrier strength, unfavorable inner and outer surfaces of particles, etc., and achieves smooth pores and desulfurization activity. and high stability
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Embodiment 1
[0023] (1) Preparation of carrier
[0024] Weigh 500 g of macroporous pseudo-boehmite dry rubber powder (dry basis content 71.5 wt%) produced by Yantai Henghui Chemical Co., Ltd., add 14 g of celadon powder, and mix evenly. Add 390 g of acetic acid solution with a concentration of 4.0 wt % into the aforementioned materials, knead it into a plastic body, and then extrude it into a cylinder with a diameter of 1.4 mm on a front-extrusion single-screw extruder. Dry at 120°C for 3.0 hours, then put it into a roasting furnace, raise it to 650°C at a rate of 180°C / hour, and keep the temperature constant for 3 hours.
[0025] (2) Handling of the carrier
[0026] Weigh 300 grams of the carrier obtained in (1) and place it in a rotating vessel, spray 250 g of deionized water on the carrier evenly at a speed of 30 mL / min, and spray water evenly on the aforementioned deionized water at a speed of 3.0 g / min. Add acetic acid. After spraying to the saturated water absorption rate of the c...
Embodiment 2
[0030] Weigh 500 g of the above-mentioned pseudo-boehmite dry rubber powder, add 14 g of safflower powder, and mix evenly. Concentration is that the acetic acid solution 400g of 3.5wt% is added in the aforementioned material, kneading becomes plastic body. Extruded, dried and roasted in the same manner as in Example 1. 250g of deionized water was evenly sprayed on the obtained alumina carrier at a speed of 30mL / min, and acetic acid was uniformly added to the aforementioned deionized water at a speed of 4.0g / min while spraying water. After spraying to the saturated water absorption rate of the carrier, airtight treatment at 60°C for 3.0 hours, and washing with clean water 3 times. Dry at 200°C for 3.0 hours. Catalyst B was obtained using the same catalyst preparation conditions as in Example 1.
Embodiment 3
[0032] Change the adding speed of acetic acid into 2.5g / min among the embodiment 1, other conditions are all identical with embodiment 1, obtain catalyst C.
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