Resource utilization method of limonite type laterite-nickel ore leachate
A technology of lateritic nickel ore and limonite, which is applied in the field of resource utilization of ferric phosphate precursor and regenerated ammonium oxalate, limonite-type lateritic nickel ore leaching solution, can solve the problem of high production cost, reduce iron removal cost, reduce The number of equipment and the effect of achieving cleaner production
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Embodiment 1
[0050] The present embodiment 1 provides a limonite-type laterite nickel ore leaching solution resource utilization method, comprising the following steps:
[0051] Step 1. Measure 4 parts of 100mL limonite-type laterite-nickel ore leaching solution in four heavy iron reactors, respectively add ammonia water to adjust the pH value to 8.5, and carry out heavy iron reaction under heating and stirring conditions. After the end, the temperature was kept for 50 minutes for liquid-solid separation to obtain 4 parts of iron precipitation and 4 parts of filtrate containing ammonium oxalate; wherein, the precipitation temperature was 90° C., and the heating and stirring speed was 100 r / min.
[0052] Step 2. Divide each part of the filtrate containing ammonium oxalate in step 1 into two groups for shunting treatment; wherein, four parts of the filtrate containing ammonium oxalate in the first group are subjected to evaporation and cooling crystallization to obtain 4 parts of crystalline ...
Embodiment 2
[0063] The present embodiment 2 provides a limonite-type laterite nickel ore leaching solution resource utilization method, comprising the following steps:
[0064] Step 1. Measure 6 parts of 100mL limonite-type laterite-nickel ore leaching solution respectively in six heavy iron reactors, and add ammonia water respectively to adjust pH value to 9.0, carry out heavy iron reaction under heating and stirring conditions, and heavy iron reaction After the end, the temperature was kept for 30 minutes for liquid-solid separation to obtain 6 parts of iron precipitation and 6 parts of filtrate containing ammonium oxalate; wherein, the precipitation temperature was 100° C., and the heating and stirring speed was 150 r / min.
[0065] Step 2. Divide each part of the filtrate containing ammonium oxalate in step 1 into two groups for shunting treatment; wherein, six parts of the filtrate containing ammonium oxalate in the first group are evaporated, cooled and crystallized to obtain 6 parts ...
Embodiment 3
[0073] The present embodiment 3 provides a limonite-type laterite nickel ore leaching solution resource utilization method, comprising the following steps:
[0074] Step 1. Measure 2 parts of limonite-type laterite-nickel ore leaching solution with the same volume in two iron sinking reactors, respectively add ammonia water to adjust the pH value to 9.5, carry out iron sinking reaction under heating and stirring conditions, and sink iron. After the reaction was completed, the liquid-solid separation was carried out for 60 minutes, and 2 parts of iron precipitates and 2 parts of filtrate containing ammonium oxalate were obtained; wherein, the heating and stirring speed was 130 r / min, and the reaction temperature of heavy iron was 70 °C.
[0075] In step 2, each part of the filtrate containing ammonium oxalate in step 1 is divided into two parts for flow treatment; wherein, two parts of the filtrate containing ammonium oxalate in the first group are evaporated, cooled and crystal...
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