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Method for preparing coarse-grained aluminum hydroxide by decomposing sodium aluminate solution with ultra-low seed amount

A technology of aluminum hydroxide and sodium aluminate, which is applied in the field of aluminum metallurgy, can solve the problems of increasing equipment load, increasing seed attachment, and not effectively reducing the amount of circulating seed crystals, so as to improve particle size distribution, increase nucleation rate, reduce Effect of Seed Amount

Active Publication Date: 2021-08-06
CENT SOUTH UNIV
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

Chinese Patent Publication No. CN 104803404A, published on July 29, 2015, the name of the invention is a method for strengthening the seed fraction of supersaturated sodium aluminate solution. By adding active seed crystals and additives, the decomposition rate can be significantly improved, but there is no Effectively reduce the amount of circulating seed crystals
This not only consumes a lot of manpower, materials, and material resources, but also because the seeds have not been washed, adding a large number of seeds will undoubtedly lead to increased seed attachment and increase equipment load

Method used

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  • Method for preparing coarse-grained aluminum hydroxide by decomposing sodium aluminate solution with ultra-low seed amount
  • Method for preparing coarse-grained aluminum hydroxide by decomposing sodium aluminate solution with ultra-low seed amount
  • Method for preparing coarse-grained aluminum hydroxide by decomposing sodium aluminate solution with ultra-low seed amount

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Experimental program
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Effect test

Embodiment 1

[0031] Seed crystal preparation: take 300mL sodium aluminate solution ρ(Na 2 o k )=160g / L, ρ(Al 2 o 3 )=186.67g / L, α k =1.41) was added in 100mL sodium bicarbonate suspension (ρ(NaHCO 3 )=1000g / L), stirred at a constant temperature at 50°C for 60min, and the resulting slurry was filtered and washed to prepare seed crystals.

[0032] 900mL supersaturated sodium aluminate solution ρ(Na 2 o k )=160g / L, ρ(Al 2 o 3 )=186.67g / L, α k =1.41, ρ(Na 2 o c )=5g / L) into the seed sub-trough, add 0.5g of the prepared seed crystal while stirring, and start to decompose; the decomposition adopts constant temperature decomposition, the temperature is controlled at 55±0.5°C, and the constant temperature decomposition ends after 50 hours. At this time, the alumina The caustic ratio of the sodium solution is 3.04, and the decomposition rate is 53.62%. The decomposed slurry is filtered, and the filtrate is the seed separation mother liquor, which is returned to the dissolution process. ...

Embodiment 2

[0034] The seed crystal preparation mode is consistent with embodiment 1, and 950mL supersaturated sodium aluminate solution ρ(Na 2 o k )=155g / L, ρ(Al 2 o 3 )=175.84g / L, α k =1.45, ρ(Na 2 o c )=5g / L) into the seed sub-tank, add 0.5g of the previously prepared seed crystal while stirring, and start to decompose; the initial temperature of decomposition is 70°C, and the temperature is continuously lowered at a uniform speed for 0 to 15 hours, and the temperature drop is 10°C. For 16 to 30 hours, continuous and uniform cooling is also adopted, and the cooling range is 5°C. After that, it is decomposed at 55°C for 20 hours. After the decomposition is completed, the caustic ratio of the sodium aluminate solution is 3.21, and the decomposition rate is 54.83%. The decomposed slurry is filtered, and the filtrate is the seed separation mother liquor, which is returned to the dissolution process. The filter cake is the prepared aluminum hydroxide product. The particle size analysi...

Embodiment 3

[0036] The seed crystal preparation mode is consistent with embodiment 1, and 950mL supersaturated sodium aluminate solution ρ(Na 2o k )=165g / L, ρ(Al 2 o 3 )=179.75g / L, α k =1.51, ρ(Na 2 o c )=5g / L) into the seed sub-trough, add 1g of the previously prepared seed crystals while stirring, and start to decompose; the initial temperature of decomposition is 65°C, and the temperature is continuously lowered at a uniform speed for 0 to 7 hours, and the temperature drop range is 5°C, 8 Continuous uniform cooling is adopted for ~20 hours, and the cooling range is 5°C. Continuous uniform cooling is used for 21 to 32 hours, and the cooling range is 5°C. After that, the decomposition is continued at 50°C for 19 hours. After 51 hours of decomposition, the caustic ratio of the sodium aluminate solution was 3.31, and the decomposition rate was 54.38%. The decomposed slurry is filtered, and the filtrate is the seed separation mother liquor, which is returned to the dissolution process...

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Abstract

The invention discloses a method for preparing coarse-grained aluminum hydroxide by decomposing an ultra-low seed crystal amount of sodium aluminate solution, which belongs to the field of metallurgy technology, and comprises the following steps: 1) nucleation-agglomeration: mixing low caustic ratio sodium aluminate solution Mix evenly with the seed crystals, stir and decompose at the first decomposition temperature; 2) re-agglomeration-growth: cool down the slurry obtained in step 1), and continue to stir and decompose at the second decomposition temperature until the decomposition is completed. Coarse aluminum hydroxide products can be prepared through the above steps. The present invention uses less seed crystals, reduces production costs, and improves equipment productivity; meanwhile, the process is simple and easy to realize industrial production; the aluminum hydroxide product has a relatively coarse particle size, with an average particle size of d 50 50-80 μm.

Description

technical field [0001] The invention relates to the technical field of aluminum metallurgy, in particular to a method for preparing coarse-grained aluminum hydroxide by decomposing an ultra-low seed crystal amount of sodium aluminate solution. Background technique [0002] Sodium aluminate solution seed crystal decomposition is one of the very important processes in the production of alumina by Bayer process. It not only affects the quantity and quality of alumina products, but also directly affects production efficiency and other processes. The seed crystal decomposition process of sodium aluminate solution generally has problems such as large circulation of aluminum hydroxide seed crystals, low decomposition efficiency, difficulty in meeting the requirements of sandy alumina product particle size, many equipment, large investment, and large power consumption. Sodium aluminate The seed crystal decomposition process of the solution has always been the "bottleneck" in the pr...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C01F7/14
CPCC01F7/144
Inventor 李小斌吴心平周秋生刘桂华齐天贵彭志宏王一霖
Owner CENT SOUTH UNIV