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Mineral leaching method and mineral leaching system for ionic rare earth mine
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An ion-type rare earth ore leaching technology, applied in the field of hydrometallurgy, can solve the problems of high NaCl concentration, damage to the environment, and long leaching cycle, etc., to achieve low content of impurity elements, high rare earth leaching rate, and good leaching effect Effect
Inactive Publication Date: 2014-02-05
GANZHOU NONFERROUS METALLURGICAL RES INST
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[0004] In this technical field, the leaching agent that has been tried also has NaCl. However, its disadvantages are: the required NaCl concentration is high, the leaching cycle is long, the unit consumption is large, the content of non-rare earth impurities in the leaching solution is high, and the product quality is poor. And the tailings contain a lot of Na + , causing soil salinization and damaging the environment, it has already been eliminated
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example 1
[0031] Take ionic rare earth ore-1, ionic phase rare earth 0.097%, moisture 10.86%, use 2% ammoniumsulfate for leaching, rare earth leaching rate is 95.05%, penetration time is 6h, leaching period is 58h, leaching solution REO1.26g / L, Fe<0.001g / L, Al0.022g / L, Si0.015g / L, Ca0.280g / L, pH4.5; using the 2% leaching agent of the present invention, the rare earth leaching rate is 95.15%, and the penetration time 7.5h, leaching cycle is 60h, leaching solution REO0.94g / L, Fe<0.001g / L, Al0.019g / L, Si0.009g / L, Ca0.240g / L, pH4.5.
example 2
[0033] Take ionic rare earth ore-1, ionic phase rare earth 0.097%, moisture 10.86%, use 2% ammonium sulfate for leaching, rare earth leaching rate is 95.05%, penetration time is 6h, leaching period is 58h, leaching solution REO1.26g / L, Fe<0.001g / L, Al0.022g / L, Si0.015g / L, Ca0.280g / L, pH4.5; using the 5% leaching agent of the present invention, the rare earth leaching rate is 95.25%, and the penetration time 6h, leaching cycle is 48h, leaching solution REO1.25g / L, Fe<0.001g / L, Al0.025g / L, Si0.011g / L, Ca0.320g / L, pH4.5.
example 3
[0035]Take ionic rare earth ore-2, ionic phase rare earth 0.062%, moisture 10.69%, use 2% ammonium sulfate for leaching, the rare earth leaching rate is 92.90%, the penetration time is 5.5h, the leaching period is 56h, and the leaching solution REO0.82g / L, Fe<0.001g / L, Al0.016g / L, Si0.009g / L, Ca0.220g / L, pH4.5; using the 2% leaching agent of the present invention, the rare earth leaching rate is 93.01%, and the penetration rate is 93.01%. The time is 7.0h, the leaching period is 58h, the leaching solution is REO0.60g / L, Fe<0.001g / L, Al0.010g / L, Si0.009g / L, Ca0.144g / L, pH4.5.
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Abstract
The invention relates to a mineral leaching method for an ionic rare earth mine. The mineral leaching method is characterized by comprising the following steps: carrying out percolation leaching on the mine by taking ammonia-free electrolyte as a mineral leaching agent, so that positive ions in the mineral leaching agent and ion-phase rare earth adsorbed on the surface of a carrier mine exchange to form a soluble rare earth compound entering the solution; loading the ionic rear earth mine in a mineral leaching exchange column, and adding the ammonia-free mineral leaching agent with the concentration of 2-5% according to the proportion of the mineral leaching agent (liters) to the mine (kilograms) being 0.6-0.8; after the surface of the mine is exposed out, adding top water according to the proportion of the top water (liters) to the mine (kilograms) being about 0.2; and draining away a residual solution in the mineral leaching exchange column fundamentally, namely ending mineral leaching work. The mineral leaching method is high in mineral leaching efficiency, and can prevent the pollution of ammonianitrogen to the environment.
Description
technical field [0001] The invention relates to a leaching method and system for ionic rare earth ore, in particular to a leaching method and system for ionic rare earth ore without ammonia leaching agent and compound leaching agent, belonging to hydrometallurgy field. Background technique [0002] At present, the commonly used ionic rare earth ore leaching agent is ammoniumsulfate, which has the characteristics of low price and high rare earth leaching rate. However, this leaching agent contains NH 4 + , the use of this leaching agent to leaching ionic rare earth ore will produce a large amount of ammonia nitrogenwastewater, causing water pollution. With an annual output of 3,000 tons of rare earth (calculated as REO rare earth oxides), the treatment volume of ammoniumsulfate leaching wastewater is about 1.8 million tons per year, the ammonia nitrogendischarge is about 6,000 tons per year, and the cost of ammonia nitrogenwastewater treatment is about 25 yuan per ton....
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