Technique for producing sodium nitrate by chilisaltpeter adverse current circulation leaching
A technology of countercurrent circulation and sodium nitrate, which is applied to the preparation of alkali metal nitrate, etc., can solve the problems of high energy consumption, large water consumption, and low concentration of sodium nitrate, etc., and achieve short process flow, low production cost and simple operation Effect
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Embodiment 1
[0010] Embodiment 1: take countercurrent circulation leaching process, specifically comprise the following steps:
[0011] (1) the sodium nitrate content 6% sodium nitrate ore is crushed to particles with a particle size≤5cm with a jaw crusher;
[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 into the countercurrent leaching column from the high level tank through the bottom until the liquid level submerges the ore surface, and the leaching brine stays in the column for 10 hours; then the leaching brine containing 355g / L sodium nitrate Also after heating to 45°C, inject the countercurrent leaching column from the high level tank through the bottom, and flow the concentrated leaching solution that has stayed for 10 hours from the upper overflo...
Embodiment 2
[0016] Embodiment 2: take countercurrent circulation leaching process, specifically comprise the following steps:
[0017] (1) the sodium nitrate content 6% sodium nitrate ore is crushed to particles with a particle size≤5cm with a jaw crusher;
[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 into the countercurrent leaching column from the high level tank through the bottom until the liquid level submerges the surface of the ore, and the leaching brine stays in the column for 8 hours; then the leaching brine containing 365g / L sodium nitrate Also after heating to 65°C, inject the countercurrent leaching column from the high level tank through the bottom, and flow the concentrated leaching solution that has stayed for 8 hours from the upper ov...
Embodiment 3
[0021] Embodiment 3: The preferred embodiment is: (1) ore crushing: Sodium nitrate ore is crushed into particles with a particle size of less than or equal to 5cm; (2) countercurrent circulation leaching: the broken ore is packed into a countercurrent leaching column, and The height-to-diameter ratio of the column 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, the energy provided by the head tank or pump enters from the bottom of the countercurrent leaching column, and then It flows out from the upper overflow tank of the countercurrent leaching column, and after 3-4 stages of countercurrent cyclic leaching, the content of sodium nitrate in the leaching solution will rise from 300 to 380g / L to 390 to 500g / L. (3) Low-temperature separation, washing, and drying: After the leaching completion liquid is cooled by heat exchange with the low-temperature separation mother liquid, the temperatu...
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