Method for preparing high-and-middle-class ceramic kaolin from kaolin scavenging tailings
A kaolin, medium-to-high-end technology, applied in the field of non-metallic ore processing, can solve the problems of heavy iron removal burden, inefficient use of resources, high energy consumption of machine drums, etc., and achieve low production cost, large processing capacity and high classification efficiency Effect
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Embodiment 1
[0026] Example 1: A method for preparing kaolin for medium and high-grade ceramics by using kaolin to sweep tailings, including the following steps.
[0027] (1) Add the kaolin scavenging tailings to the ball mill separately, and control the slurry concentration at 50.0%, ball milling for 100 minutes; (2) Add water to the ball milled kaolin scavenging tailings to mash and disperse, control the concentration to 35.0%, and enter the slurry The pressure filter 2.5PMa first enters the FX-PU-150 hydrocyclone for rough selection, and the overflow directly enters the FX-PU-75 hydrocyclone for selection, and the 325 mesh coarse concentrate is recovered; (3) 325 will be recovered The coarse mesh concentrate is added with 0.1% of the dry amount of dispersant sodium hexametaphosphate, the concentration is 15.0%, and the flow rate is 10.0m3 / h into the high-gradient magnetic separator for magnetic separation and iron removal to obtain 325 mesh magnetic separation concentrate slurry; (4) Use t...
Embodiment 2
[0029] Example 2: A method for preparing kaolin for medium and high-grade ceramics by using kaolin to sweep tailings, including the following steps.
[0030] (1) Put the kaolin scavenging tailings and whoever into the ball mill separately, and control the slurry concentration at 55.0%, ball milling for 120 minutes; (2) Add water to the ball milled kaolin scavenging tailings to mash and disperse, control the concentration to 35.0%, and enter the slurry The press filter 2.5PMa first enters the FX-PU-150 hydrocyclone for rough selection, and the overflow directly enters the FX-PU-75 hydrocyclone for selection, and 325 mesh coarse concentrate is recovered; (3) 325 will be recovered The coarse mesh concentrate is added with 0.23% of the dry content of dispersant sodium hexametaphosphate, the concentration is 15.0%, and the flow rate is 8.0m3 / h into the high-gradient magnetic separator for magnetic separation and iron removal to obtain 325 mesh magnetic separation concentrate slurry; (...
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