A kind of heavy oil hydrogenation catalyst and preparation method thereof
A heavy oil hydrogenation and catalyst technology, applied in catalyst carriers, chemical instruments and methods, metal/metal oxide/metal hydroxide catalysts, etc., can solve the problems of low production efficiency, long drying time, dust pollution, etc. The effect of improving production efficiency, avoiding water addition and reducing energy consumption
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[0021] 1. The preparation method of pseudo-boehmite adopts the pH swing gelation method, and the specific process includes the following steps:
[0022] a) Prepare an aqueous acidic aluminum salt solution, with Al in the solution 2 o 3 The metered concentration is 2~10g / 100ml;
[0023] b) prepare alkaline aluminate aqueous solution, with Al in the solution 2 o 3 The calculated concentration is 8~30g / 100ml, or prepare dilute ammonia solution, NH 3 The content is 8~16 g / 100ml;
[0024] c) Add an appropriate amount of acidic aluminum salt solution to the neutralized bottom water to lower the pH value to 2.0-4.0, preferably 3.0-4.0, most preferably 3.0-3.5, and the solution temperature is 50-95°C, preferably 55 ~75°C, the most suitable is 60~70°C; stop adding the acidic aluminum salt solution and stabilize for 3~10 minutes;
[0025] d) The acidic aluminum salt aqueous solution and the alkaline aluminate aqueous solution are continuously added to the step (c) at the same time...
Embodiment 1
[0037] 2L sodium metaaluminate aqueous solution (with Al 2 o 3 The concentration is 15g / 100mL) and 3L aluminum sulfate aqueous solution (as Al 2 o 3 The concentration of the meter is 3g / 100mL) and put them into the container at the high position respectively, and the flow meter flows into the stainless steel container equipped with a 6L clean water belt agitator and a heating mantle, and heats to 60°C; Aluminum sulfate solution, reduce the pH value of the slurry to 3.0, and after stabilizing for 10 minutes, add the two materials into the stainless steel tank at a certain speed at the same time, keep the pH value at 7.3, and neutralize the gelling reaction for 15 minutes. Then stop adding aluminum sulfate solution, so that the pH value rises to 9.2, stop adding sodium metaaluminate solution, and stabilize for a period of time; pass through aluminum sulfate solution, reduce the pH value of the slurry to 3.0, and stabilize for a period of time; pass through sodium metaaluminate...
Embodiment 2
[0040] Compared with Example 1, during the pH swing process, the solution temperature was 65°C, and the neutralized pH value was 7.0. After the slurry was filtered and washed, it was dried at 110°C for 0.8 hours, and the dry basis content of the material was 45%. Other materials The dosage and operating conditions were the same as those in Example 1 to prepare catalyst C-B. Carrier B was saturated and impregnated with solution L-1, dried at 110°C for 2 hours, and calcined at 500°C for 3 hours to obtain catalyst C-A.
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