Spherical cobalt carbonate with large particle size and its synthesis method
A synthesis method and technology of cobalt carbonate, applied in the direction of cobalt carbonate, etc., to achieve the effects of short synthesis time, improved utilization rate, and continuous and controllable process
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Embodiment 1
[0035] Step S1: Prepare a cobalt sulfate solution with a concentration of 1.5 mol / L and an ammonium bicarbonate solution with a concentration of 2.5 mol / L;
[0036] Step S2: Use 0.5 mol / L ammonium bicarbonate solution as the base liquid, the volume of the bottom liquid accounts for 60% of the total volume of the synthesis tank, and the stirring blade of the synthesis tank is a disc turbine type stirring. Adjust the reaction temperature of the system to 40°C, and the linear stirring speed to 4m / s. Add the cobalt sulfate solution and the ammonium bicarbonate solution into the reaction kettle concurrently, wherein the flow rate of the cobalt sulfate solution is 2L / h, and the ammonium bicarbonate solution controls the pH of the reaction system to be 7.7~7.8. The total feeding time of the control system is 80h and the feeding is stopped when the particle size is 8.2±0.2μm, and the centrifuge is dried for later use;
[0037] Step S3: Weigh 5 kg of the seed crystal obtained in step ...
Embodiment 2
[0041] Step S1: Prepare a cobalt sulfate solution with a concentration of 1.5 mol / L and an ammonium bicarbonate solution with a concentration of 2.5 mol / L;
[0042] Step S2: Use 1.0 mol / L ammonium bicarbonate solution as the base liquid, the volume of the base liquid accounts for 30% of the total volume of the synthesis tank, and the stirring blade of the synthesis tank is a disc turbine type stirring. Adjust the reaction temperature of the system to 45°C, and the linear stirring speed to 5m / s. Add the cobalt sulfate solution and the ammonium bicarbonate solution into the reaction kettle concurrently, wherein the flow rate of the cobalt sulfate solution is 3L / h, and the ammonium bicarbonate solution controls the pH of the reaction system to be 7.6~7.7. When the total feeding time of the control system is 100h and the particle size is 9.8±0.2μm, the feeding is stopped, and the centrifugal drying is used for later use;
[0043] Step S3: Weigh 8 kg of the seed crystal obtained i...
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