Reverse flotation process for synchronously removing magnesium and aluminum in phosphorite
A reverse flotation, magnesium-aluminum technology, used in flotation, solid separation and other directions, can solve the problems of negative impact of sorting, and achieve the effect of better fluidity, convenient transportation and strong adaptability
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Embodiment 1
[0023] A reverse flotation process for simultaneous removal of magnesium and aluminum in phosphate rock. The specific steps of the method described in this embodiment are:
[0024] (1) Put P 2 O 5 Grade 29.0%, MgO content 1.6%, Al 2 O 3 Phosphate pulp with a content of 3.0%, a particle size of less than 0.074mm accounting for 64.0%, and a pulp concentration of 30.0wt% is introduced into the synchronous reverse flotation process; a regulator (sulfuric acid and aluminum sulfate in a molar ratio of 7.0:1.0) is added to the phosphate pulp. mixture), the amount of addition is 6.9kg / t; then add fatty acid collectors (sodium salt of oleic acid, linoleic acid, palmitic acid, stearic acid to the phosphate slurry at a mass ratio of 4.5:1.0 to The mixture of mass ratio 14:10:14:62 composition) and amine collector (dodecylamine acetate), the total amount of collector addition is 0.3kg / t, carries out pre-flotation, obtains product I in the tank and foam product I, which is phosphorus ...
Embodiment 2
[0033]A reverse flotation process for simultaneous removal of magnesium and aluminum in phosphate rock. The specific steps of the method described in this embodiment are:
[0034] (1) Put P 2 O 5 Grade 26.2%, MgO content 1.64%, Al 2 O 3 Phosphate pulp with a content of 3.8%, a particle size of less than 0.074mm, accounting for 76.0%, and a pulp concentration of 25.0wt% is introduced into the synchronous reverse flotation process; a modifier (sulfuric acid and aluminum sulfate in a molar ratio of 6.0:1.0) is added to the phosphate pulp. mixture), the addition amount is 9.6kg / t; then add fatty acid collectors (sodium salt of oleic acid, linoleic acid, palmitic acid, stearic acid to the phosphate slurry at a mass ratio of 4.0:1.0 to The mixture of mass ratio 14:10:14:62 composition) and amine collector (dodecylamine acetate), the total amount of collector added is 0.44kg / t, carries out pre-flotation, obtains product I in the tank and foam product I, which is phosphorus taili...
Embodiment 3
[0043] A reverse flotation process for simultaneous removal of magnesium and aluminum in phosphate rock. The specific steps of the method described in this embodiment are:
[0044] (1) Put P 2 O 5 Grade 24.0%, MgO content 2.29%, Al 2 O 3 Phosphate pulp with a content of 3.76%, a particle size of less than 0.074mm accounting for 80.0%, and a pulp concentration of 35.0wt% is introduced into the synchronous reverse flotation process; a regulator (sulfuric acid and aluminum sulfate in a molar ratio of 4.0:1.0) is added to the phosphate pulp. mixture), the addition amount is 9.9kg / t; then add fatty acid collectors (sodium salt of oleic acid, linoleic acid, palmitic acid, stearic acid to the phosphate slurry at a mass ratio of 3.5:1.0 to The mixture of mass ratio 14:10:14:62 composition) and amine collector (dodecylamine acetate), the total amount of collector added is 0.60kg / t, carries out pre-flotation, obtains product I in the tank and foam product I, which is phosphorus tai...
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