The invention relates to a
branch flotation technology for collophanite, which comprises the following steps: crushing and
grinding silicon calcium collophanite ores, and then adding water and mixing into
slurry, and guiding the
slurry to flow into a flotation groove; adding a
regulator and a collecting agent for mixing the
slurry, and then pouring into a
reverse flotation system for performing
reverse flotation, wherein products in the groove are
reverse flotation concentrates; grading the reverse flotation concentrates into coarse fraction and fine fraction; pouring the coarse fraction partinto a desilicification reverse flotation groove, adding a desilicification
regulator and a desilicification collecting agent for mixing the slurry, and then pouring into a desilicification
system for performing reverse flotation, wherein products in the groove are desilicification reverse flotation concentrates; pouring the fine fraction part into a normal flotation groove, adding a normal flotation pH (Potential of
Hydrogen)
regulator, the regulator and the collecting agent for mixing the slurry, and then performing normal flotation, wherein foam products of the normal flotation are normal flotation concentrates; mixing the normal flotation concentrates with the desilicification reverse flotation concentrates, thereby forming the final
phosphorus concentrates; and concentrating, filtering and
drying, thereby obtaining
phosphorus concentrates. The
branch flotation technology for collophanite has the advantages that the separation efficiency is high, the technic index is excellent, the content of MgO in the obtained
phosphorus concentrates is lower, the quality of the concentrates is high, and the comprehensive cost of the final product of the
phosphor concentrates is lower.