Technique for producing sodium nitrate by chilisaltpeter adverse current circulation leaching
A countercurrent circulation, sodium nitrate technology, applied in the preparation of alkali metal nitrates and other directions, can solve the problems of large water consumption, high energy consumption of sodium nitrate, low concentration of sodium nitrate, etc., and achieves low production cost, short technological process, and simple operation. Effect
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Embodiment 1
[0010] Example 1: Adopting the countercurrent circulation leaching process, specifically including the following steps:
[0011] (1) Crush the sodium saltpetre ore with a sodium nitrate content of 6% with a jaw crusher to particles with a particle size of ≤5cm;
[0012] (2) Pack the crushed ore into a countercurrent leaching column with a height-to-diameter ratio of 5, until the ore is flush with the top of the leaching column, and heat the prepared leaching brine containing 355g / L of sodium nitrate to 45 After ℃, the leaching brine is injected from the high tank through the bottom into the countercurrent leaching column until the liquid level floods the surface of the ore. The leaching brine stays in the column for 10 hours; then the leaching brine containing 355g / L sodium nitrate After the same heating to 45°C, inject the countercurrent leaching column from the upper tank through the bottom, and flow the leaching concentrate that stayed for 10 hours from the upper overflow tank ...
Embodiment 2
[0016] Example 2: Adopting the countercurrent circulating leaching process, specifically including the following steps:
[0017] (1) Crush the sodium saltpetre ore with a sodium nitrate content of 6% with a jaw crusher to particles with a particle size of ≤5cm;
[0018] (2) Pack the crushed ore into a countercurrent leaching column with a height-to-diameter ratio of 3 until the ore is flush with the top of the leaching column, and heat the prepared leaching brine containing 365g / L of sodium nitrate to 65 After ℃, the leaching brine is injected from the high tank through the bottom into the countercurrent leaching column until the liquid level submerges the surface of the ore. The leaching brine stays in the column for 8 hours; then the leaching brine containing 365g / L sodium nitrate After the same heating to 65°C, inject the countercurrent leaching column from the upper tank through the bottom, and flow the leaching concentrate that stayed for 8 hours from the upper overflow tank ...
Embodiment 3
[0021] Example 3: The preferred implementation is: (1) Ore crushing: crushing sodium saltpeter ore into particles with a particle size of ≤ 5cm; (2) Countercurrent cyclic leaching: The crushed ore is loaded into a countercurrent leaching column, and then leached. The column height to diameter ratio should be in the range of 1 to 5, preferably 3 to 4. After the adjusted low-temperature separation mother liquor is heated to 45°C to 60°C, its energy is supplied from the bottom of the countercurrent leaching column by a high tank or pump, and then From the overflow tank on the upper part of the countercurrent leaching column, after 3-4 stage countercurrent leaching, the content of sodium nitrate in the leaching solution will rise from 300~380g / L to 390~500g / L. The leaching at this time The liquid is the finished leaching solution; (3) Low-temperature separation, washing, and drying: After the finished leaching solution is cooled by heat exchange with the low-temperature separation mot...
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