Monolithic catalyst for use in preparation of chloride by using hydrogen chloride and preparation method thereof
A monolithic catalyst, hydrogen chloride technology, applied in the direction of chloride preparation, catalyst activation/preparation, metal/metal oxide/metal hydroxide catalyst, etc., can solve the problem of low catalyst activity, and achieve a simple and high-efficiency synthesis method Conversion rate, solve the effect of low activity
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Embodiment 1
[0031] (1) 12.4g RuCl 3 ·3H 2 O was dissolved in 96ml of ethylene glycol, slowly heated to 140°C, and 220ml of 1mol L was added dropwise -1 K 2 CO 3 The aqueous solution was stirred with nitrogen for 5h, transferred to an autoclave at 100°C, crystallized for 10h, filtered, dried, and calcined at 260°C to obtain about 7.7g RuO 2 ·3H 2 O(110), wherein the (110) crystal plane accounts for 40%;
[0032] (2) 7.7g RuO 2 ·3H 2 O(110) was loaded onto 5.4 g of SBA-15 by wet impregnation, washed with ethanol, and dried to form 10% RuO 2 (110) / SBA-15, the RuO 2 (110) / SBA-15 is ground into powder, adding γ-Al 2 o 3 Sol (containing γ-Al 2 o 3 about 6g) and 10ml 1mol L -1 HNO 3 , with magnetic stirring for 5 hours, RuO 2 (110) content is the active slurry of 5wt%;
[0033] (3) Grind the FeCrAl alloy with sandpaper to increase the surface roughness, and put it in 1mol L -1 Ultrasonic washing in NaOH solution for 30 minutes to remove surface impurities and oil stains, washin...
Embodiment 2
[0038] The ethylene glycol in the embodiment 1 step (1) is changed into the 20% arginine solution of 300ml, K 2 CO 3 Change to NaOH, change the temperature into the autoclave to 140°C, change the crystallization time to 12h, change the roasting temperature to 320°C, and replace SBA-15 with rutile TiO in step (2). 2 , the calcination temperature in step (4) was changed to 450°C, the calcination temperature in step (5) was changed to 600°C, and other conditions remained unchanged, RuO 2 (110) / TiO 2 / FeCrAl, in which (110) crystal plane accounts for 49%. Under the same conditions, the conversion rate of hydrogen chloride was 94.2%. Example 3:
Embodiment 3
[0039] The ethylene glycol in embodiment 1 step (1) is changed into 20wt% cetyl trimethyl ammonium bromide solution (ethylene glycol is identical with the molar weight of cetyl trimethyl ammonium bromide), K 2 CO 3 Change to potassium hydroxide, change the temperature of the autoclave to 60°C, change the roasting temperature to 220°C, replace SBA-15 with MCM-41 in step (2), and change the temperature of cordierite at 1mol L -1 HNO 3 Soak in water for 30min, take out, wash and dry. In step (4), FeCrAl is replaced by cordierite, the roasting temperature is changed to 450°C, the roasting temperature in step (5) is changed to 600°C, and other conditions remain unchanged, and RuO 2 (110) / MCM-41 / cordierite, in which the (110) crystal plane accounts for 39%. The conversion rate of hydrogen chloride was 84.9% under the same conditions.
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