Settling agent in wet-method phosphoric acid concentration processing process
A treatment process, wet-process phosphoric acid technology, applied in the direction of phosphorus compounds, chemical instruments and methods, inorganic chemistry, etc., can solve the problems of high solid content and impurity ion content, increasing difficulty, large number of storage tanks, etc., to achieve clear and bright texture , shorten the settling time, the effect of low impurity content
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Embodiment 1
[0015] The settling agent is prepared by stirring and mixing sodium dodecyl sulfonate, polyacrylamide, diatomaceous earth and sodium carbonate in a stirring tank in parts by mass of 40 parts, 16 parts, 25 parts and 12 parts respectively. At 0.23kg / t(P 2 o 5 Calculated) the amount of concentrated wet-process phosphoric acid is added, after 14 hours of sedimentation, the removal rate of fluorine reaches 87%, Fe 3+ The removal rate reaches 17%, Al 3+ The removal rate reaches 15%, Mg 2+ The removal rate reached 22%, Ca 2+ The removal rate reaches 10%, Si 4+ The removal rate reaches 19%, and the obtained wet-process phosphoric acid is clear and bright.
Embodiment 2
[0017] The settling agent is prepared by stirring and mixing sodium polyacrylate, polyvinyl alcohol, bentonite and sodium hydroxide in a stirring tank in parts by mass of 85 parts, 20 parts, 35 parts and 16 parts respectively. At 0.27kg / t(P 2 o 5 Calculated) the amount of concentrated wet-process phosphoric acid is added, after 12 hours of sedimentation, the removal rate of fluorine reaches 92%, Fe 3+ The removal rate reaches 18%, Al 3+ The removal rate reached 21%, Mg 2+ The removal rate reached 24%, Ca 2+ The removal rate reached 27%, Si 4+ The removal rate reaches 16%, and the obtained wet-process phosphoric acid is clear and bright.
Embodiment 3
[0019] The settling agent is prepared by stirring and mixing alkylbenzenesulfonic acid, polyoxyethylene, activated carbon and sodium chloride in parts by mass of 92 parts, 28 parts, 35 parts and 18 parts respectively in a stirring tank. At 0.29kg / t(P 2 o 5 Calculated) the amount of concentrated wet-process phosphoric acid is added, after settling for 10 hours, the removal rate of fluorine reaches 88%, Fe 3+ The removal rate reaches 13%, Al 3+ The removal rate reached 16%, Mg 2+ The removal rate reached 21%, Ca 2+ The removal rate reached 18%, Si 4+ The removal rate reaches 23%, and the obtained wet-process phosphoric acid is clear and bright.
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