Non-noble metal mercury-free catalyst for acetylene hydrochlorination reaction, preparation method and application thereof
A technology of acetylene hydrochlorination and non-precious metals, which is applied in the direction of metal/metal oxide/metal hydroxide catalyst, physical/chemical process catalyst, hydrogen halide addition preparation, etc., which can solve the problem of high cost and difficult large-scale industrial production, catalyst The loss of active components, intense reaction and other problems, to achieve good catalytic stability, single-pass conversion rate reduction, high and low temperature activity effect
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Embodiment 1
[0051] (1) Weigh 17.05g CuCl 2 2H 2 O, 2.67 g NH 4 Cl and 5.76 g 85% H 3 PO 4 Dissolve in 43g of deionized water to prepare CuCl 2 , NH 4 Cl and H 3 PO 4 The solution;
[0052] (2) Set the specific surface area to 700-1300m 2 / g, the carbon tetrachloride adsorption value is 55-65%, and the ash value is less than 6%. The granular activated carbon after pickling is soaked in the above-mentioned prepared solution at room temperature, and the volume ratio of the control solution to the activated carbon is 0.5:1. , soak for 2 hours;
[0053] (3) Dry the soaked activated carbon and dry it with hydrogen chloride gas at 100°C to obtain the required catalyst A1.
[0054] (4) The above-mentioned catalyst is loaded into the tube reactor, and the C 2 h 2 Mixed gas with HCl (C 2 h 2 and HCl molar ratio of 1:1.05) for hydrochlorination reaction, control the reaction temperature at 80°C, and the acetylene space velocity at 20h -1 , the reaction gauge pressure is 0.1MPa, the in...
Embodiment 2
[0056] (1) Weigh 17.05g CuCl 2 2H 2 O, 1.07 g NH 4 Cl and 9.2 g 85% H 3 PO 4 Dissolve in 80g of deionized water to prepare CuCl 2 , NH 4 Cl and H 3 PO 4 The solution;
[0057] (2) Set the specific surface area to 700-1300m 2 / g, the carbon tetrachloride adsorption value is 55~65%, the granular activated carbon after pickling is less than 6% is soaked in the above-mentioned prepared solution, and the control soaking temperature is 40 ℃, the volume ratio of solution and activated carbon is less than 6%. 1:1, soak for 10 hours;
[0058] (3) Dry the soaked activated carbon and dry it with hydrogen chloride gas at 150° C. to obtain the required catalyst A2.
[0059] (4) The above-mentioned catalyst is loaded into the tube reactor, and the C 2 h 2 Mixed gas with HCl (C 2 h 2 The molar ratio of HCl and HCl is 1:1) for hydrochlorination reaction, the temperature of the reaction is controlled at 100°C, and the space velocity of acetylene is 50h -1 , the reaction gauge pr...
Embodiment 3
[0061] (1) Weigh 17.05g CuCl 2 2H 2 O, 6.42 g NH 4 Cl and 6.92 g 85% H 3 PO 4 Dissolve in 100g of deionized water to prepare CuCl 2 , NH 4 Cl and H 3 PO 4 The solution;
[0062] (2) Set the specific surface area to 700-1300m 2 / g, the carbon tetrachloride adsorption value is 55~65%, and the granular activated carbon after pickling is less than 6% is soaked in the above-mentioned prepared solution, and the control soaking temperature is 60 ℃, and the volume ratio of solution and activated carbon is: 1.5:1, soak for 5 hours;
[0063] (3) Dry the soaked activated carbon and dry it with hydrogen chloride gas at 200°C to obtain the desired catalyst A3.
[0064] (4) The above-mentioned catalyst is loaded into the tube reactor, and the C 2 h 2 Mixed gas with HCl (C 2 h 2 The molar ratio of HCl and HCl is 1:1.03) for hydrochlorination reaction, the temperature of the reaction is controlled at 120°C, and the space velocity of acetylene is 40h -1 , the reaction gauge pres...
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