High-efficiency composite catalyst for preparing acrylic acid by using lactic acid for catalytic dehydration and preparation method and application of high-efficiency composite catalyst
A composite catalyst and catalytic dehydration technology, applied in the field of catalytic chemistry, can solve problems that have not been reported in research, achieve high selectivity and maintain stability
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Embodiment 1
[0021] Weigh a certain amount of HZSM-5 molecular sieve, and roast it at 550°C for 4h; the calcined HZSM-5 molecular sieve is desiliconized and modified with 0.5M sodium hydroxide solution in 80°C aqueous solution at a liquid-solid ratio of 7.5mL / g, and then washed with water , dry; then use 0.05mol / L Ca(NO 3 ) 2 The solution was treated in a water bath at 30°C for 8 hours, washed with water, dried, and calcined; finally, the calcined molecular sieve was treated with 0.6mol / L Na 2 HPO 4 The solution was further modified and dried to obtain the desired catalyst.
[0022] Weigh 1.5 g of the above-mentioned catalyst and load it into a fixed-bed reactor with an inner diameter of 8 mm and a height of 360 mm, and the upper and lower parts of the catalyst are filled with inert and uniform small ceramic balls. Reaction temperature 375°C, carrier gas N 2 The flow rate is 35mL / min, and the space velocity is 1.3h -1 , the concentration of the feed solution is 40wt%, and in the dehyd...
Embodiment 2
[0024] Weigh a certain amount of HZSM-5 molecular sieve, and roast it at 550°C for 4h; the calcined HZSM-5 molecular sieve is desiliconized and modified with 0.5M sodium hydroxide solution in 80°C aqueous solution at a liquid-solid ratio of 7.5mL / g, and then washed with water , dry; and then this molecular sieve is mixed with 0.05mol / L CaCl according to the same liquid-solid ratio 2 The solution was treated in a water bath at 30°C for 8 hours, washed with water, and dried; finally, the roasted molecular sieve was treated with 0.6mol / L Na 2 HPO 4 The solution was further modified and dried to obtain the desired catalyst.
[0025] Weigh 1.5 g of the above-mentioned catalyst and load it into a fixed-bed reactor with an inner diameter of 8 mm and a height of 360 mm, and the upper and lower parts of the catalyst are filled with inert and uniform small ceramic balls. Reaction temperature 390°C, carrier gas N 2 The flow rate is 35mL / min, and the space velocity is 1.3h -1 , the co...
Embodiment 3
[0027]Weigh a certain amount of HZSM-5 molecular sieve, and roast it at 550°C for 4h; the calcined HZSM-5 molecular sieve is desiliconized and modified with 0.5M sodium hydroxide solution in 80°C aqueous solution at a liquid-solid ratio of 7.5mL / g, and then washed with water , dry; and then this molecular sieve with 0.05mol / L of BaCl according to the same liquid-solid ratio 2 The solution was treated in a water bath at 30°C for 8 hours, washed with water, and dried; finally, the roasted molecular sieve was treated with 0.6mol / L Na 2 HPO 4 The solution was further modified and dried to obtain the desired catalyst.
[0028] Weigh 1.5 g of the above-mentioned catalyst and load it into a fixed-bed reactor with an inner diameter of 8 mm and a height of 360 mm, and the upper and lower parts of the catalyst are filled with inert and uniform small ceramic balls. Reaction temperature 365°C, carrier gas N 2 The flow rate is 35mL / min, and the space velocity is 1.3h -1 , the concentra...
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