Method for directly producing potassium nitrate end product from complex nitrate bittern
A technology of nitrate and potassium nitrate, applied in the directions of alkali metal nitrate preparation and energy input, can solve the problems of undiscovered high-quality potassium nitrate finished product, large water consumption, large potassium loss, etc., and achieves white color, energy efficiency and utilization rate. High, reduce potassium loss effect
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Embodiment 1
[0022] The brine composition of a certain salt lake is K + 0.41%, Mg 2+ 0.30%, Ca 2+ 0.048%, Na + 10.19%, Cl - 15.57%, SO 4 2- 1.64%, NO 3 2- 0.64%, with this brine as raw material:
[0023] (1) Import the brine into the salt field, use solar energy to evaporate and crystallize the brine in sections, control the mass fraction of sulfuric acid radicals in the brine discharged from the frozen nitric acid pool to be 0.05%, and the content of potassium ions in the sodium salt pool to be 4.3% by mass; (2) import the brine into Settling tank, add sodium hydroxide at 50g per cubic meter of halogen, stir for 2 hours, heat to 55°C, add sodium carbonate at 2g per cubic meter of halogen, and settle for 12 hours; (3) Halogen formation and steps after removing impurities (6) The second-effect high-temperature salt discharge is brine according to the mass ratio: salt discharge = 4:1 countercurrent mixing, and the residual potassium in the high-temperature discharge salt is wa...
Embodiment 2
[0026] The brine composition of a certain salt lake is K + 0.35%, Mg 2+ 0.36%, Ca 2+ 0.04%, Na + 10.49%, Cl- 14.96%, SO 4 2- 2.34%, NO 3 2- 1.82%, with this brine as raw material:
[0027] (1) Import the brine into the salt field, use solar energy to evaporate and crystallize the brine in stages, control the mass fraction of sulfate radicals in the brine discharged from the frozen nitrification tank to be 0.4%, and the content of potassium ions in the brine to be 4.1% by mass; (2) Import the brine into the sedimentation tank , add sodium hydroxide by 50g per cubic meter of halogenation, stir for 2 hours, heat to 60°C, add sodium carbonate by 3g per cubic meter of halogenation, and settle for 18 hours; (3) halogenation and step (6) after removing impurities ) II effect high-temperature desalting according to the mass ratio into brine: desalting = 4.1:1 countercurrent mixing, using brine to wash out the residual potassium in the high-temperature desalting, so that ...
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