A method for preparing modified alumina carrier by using water-reactive halide
A technology of alumina carrier and alumina, which is applied in the direction of catalyst carrier, chemical instruments and methods, silicon compounds, etc., can solve the problems of complicated mechanism of action, difficulty in large-scale industrial production, destruction, etc., and achieve low cost and easy large-scale The effect of popularization and application and simple operation process
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Embodiment 1
[0028] Example 1: Fill 0.5kg of pseudo-boehmite (produced by Aluminum Corporation of China Shandong Branch, P-DF-03, ignition loss ≤ 24%) in a glass-lined fixed-bed reactor, and use dry nitrogen at 40°C Under purge for 0.2h, the space velocity of nitrogen is 300h -1 ; With dry nitrogen as the purge gas, the reactor pressure is 0.1MPa (absolute pressure), the fixed bed reactor is heated at a rate of 2°C / min, and when the reactor temperature rises to 50°C, nitrogen is used to bubble The method carries water-reactive halide silicon tetrachloride to interact with pseudoboehmite, the temperature of the bubbler is 35°C, and the space velocity of nitrogen is 300h -1 ; when the reactor temperature rises to 120°C, switch to dry nitrogen for purging; when the reactor temperature rises to 450°C, stop heating up, and after roasting at 450°C for 5 hours, cool to room temperature to obtain a concentrated pore size distribution The porous alumina carrier, its pore structure parameters are s...
Embodiment 2
[0029] Example 2: Fill 0.5kg boehmite (manufactured by Zibo Baida Chemical Co., Ltd., BD-BS03, alumina content ≥ 83%) into a glass-lined fixed-bed reactor, blow with dry nitrogen at 35°C Sweep for 0.5h, the space velocity of nitrogen is 400h -1 ; With dry nitrogen as the purge gas, the reactor pressure is 0.12MPa (absolute pressure), the fixed bed reactor is heated at a rate of 4°C / min, and when the reactor temperature rises to 60°C, nitrogen bubbles are used The method carries the water-reactive halide titanium tetrachloride to interact with boehmite, the temperature of the bubbler is 35 ℃, and the space velocity of nitrogen is 400h -1 ; When the reactor temperature rises to 130°C, switch to dry nitrogen for purging; when the reactor temperature rises to 550°C, stop heating up, and after roasting at 350°C for 8 hours, cool to room temperature to obtain a concentrated pore size distribution The porous alumina carrier, its pore structure parameters are shown in Table 1.
Embodiment 3
[0030] Example 3: Pack 0.5kg of boehmite (manufactured by Zibo Baida Chemical Co., Ltd., BD-BS03, with alumina content ≥ 83%) in a glass-lined fixed-bed reactor, and purge with dry nitrogen at 40°C 0.5h, the space velocity of nitrogen is 300h -1 ; With dry nitrogen as the purge gas, the reactor pressure is 0.15MPa (absolute pressure), the fixed bed reactor is heated at a rate of 10°C / min, and when the reactor temperature rises to 50°C, nitrogen is used to bubble The way to carry the water-reactive halide tin tetrachloride to interact with boehmite, the temperature of the bubbler is 50 ℃, and the space velocity of nitrogen is 600h -1 ; when the reactor temperature rises to 150°C, switch to dry nitrogen for purging; when the reactor temperature rises to 550°C, stop heating, and after roasting at 550°C for 4 hours, cool to room temperature to obtain a concentrated pore size distribution The porous alumina carrier, its pore structure parameters are shown in Table 1.
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