Detailed Explanation of Preparation Method of Ultrafine Aluminum Hydroxide

A superfine aluminum hydroxide preparation method, the sodium aluminate NaAlO2 solution and carbon dioxide containing gas touch, under the condition of high gravity carbonization reaction preparation of aluminum hydroxide gel, and then get different crystal type of ultrafine aluminum hydroxide, mainly by carbonization, filtration, washing, drying process.

a superfinealuminum hydroxidePreparation method, the sodium aluminate NaAlO2 solution and containing carbon dioxide gas touch, under the condition of high gravity carbonation reaction of preparation of aluminum hydroxide gel, and then get different crystal type of ultrafine aluminum hydroxide, mainly by carbonation, filtration, washing, boring process.
This preparation method can use the central commodity NaAlO2 solution and CO2 waste gas, using the spiral channel type rotating bed RBHC for carbonization reaction as the primary technology to prepare nano-scale ultrafine aluminum hydroxide, to solve the traditional mixing tank method of CO2 gas absorption rate is low, carbonization time is long, commodity purity is low, particle size is not uniform and rotating packed bed RPB carbonization reaction is easy to block and other technical problems. The nano-scale ultrafine fibrous and granular aluminum hydroxide with different crystal forms were prepared. The granular aluminum hydroxide of about 10nm prepared by the invention can be used as an outstanding inorganic flame retardant, and the prepared nanofibrous pseudo-boehmite with a particle size of about 5nm and a length of 200-300nm can be widely used in the catalytic field.
1. A preparation method of ultrafine aluminum hydroxide, touching sodium aluminate NaAlO2 solution and carbon dioxide-containing gas, preparing pseudo-boehmite gel by carbonization reaction method under high gravity conditions, and then obtaining ultrafine aluminum hydroxide with different crystal forms, which is mainly composed of carbonization, filtration, washing and drying processes, and is characterized in that:
1) the concentration of sodium aluminate NaAlO2 solution was controlled to 0.05 ~ 2mol/L;
2) in sodium aluminate NaAlO2 solution to participate in the mass content of 1 ~ 2% organic polymer dispersant;
3) Put the above mixture into the reactor, start up the reactor, after the liquid flow in the reactor is stable, introduce CO2 gas with concentration into the reactor, control the reactor speed to 200~3000rpm, the gas-liquid ratio to 0.5~20, control the carbonation reaction temperature to 0~100 ℃, record the temperature and pH value on time, and stop introducing CO2 gas when the pH value reaches 9~12, the speed of the reactor is decreased and recirculated for a period of time to obtain the precursor of aluminum hydroxide;
4) Continue to further dispose of the above commodities with different crystal forms, such as whether it is a process of demand aging; The above-mentioned reactor is a rotating bed super-gravity reactor, which mainly includes a rotor, a spreader arranged in the center of the rotor, a liquid inlet, an air inlet, a waste gas outlet and a material outlet.

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