Method for continuously producing large-Fisher-particle-size cobalt powder
A technology with high production cost and particle size, applied in the field of cobalt powder production, can solve the problems of uneven particle size distribution of cobalt powder, influence of particle size distribution of cobalt powder, difficulty in obtaining cobalt powder, etc. Responsive effect
- Summary
- Abstract
- Description
- Claims
- Application Information
AI Technical Summary
Problems solved by technology
Method used
Image
Examples
Embodiment 1
[0050] figure 1 It is a schematic diagram of a device for continuously producing large Fibonacci cobalt powder. Such as figure 1 As shown, the device for producing cobalt powder with a large Fischer particle size includes a flowmeter 1, a reactor 2, an agitator 3 and an agitator blade 4; wherein, the flowmeter 1 is used to control the flow of each corresponding material, and the agitator 3 is used for Add the material in the reactor 2 with stirring.
[0051] figure 2 It is a flow chart of a method for continuously producing cobalt powder with a large Fibonacci particle size. Such as figure 2As shown, a method for continuously producing cobalt powder with a large Fibonacci particle size comprises the following steps: 1) configuring a cobalt salt solution; 2) opening a constant temperature water tank, heating the water to 55-70°C, and feeding it into the external heating system of the reactor (circulation water heating), keep the temperature in the kettle at 55-70°C; 3) a...
Embodiment 2
[0059] 1) prepare cobalt chloride solution, hydrazine hydrate solution and ammoniacal liquor of certain concentration, the molar concentration of cobalt ion in the cobalt chloride solution is 1mol / L, the hydrazine hydrate concentration is 20%, and the ammoniacal liquor concentration is 30%;
[0060] 2) Add 1L of pure water bottom liquid into the 10L reaction kettle, the bottom liquid just covers the blade of the agitator, open the constant temperature water tank, heat the water to 60°C, and pass it into the external heating system of the reaction kettle;
[0061] 3) Turn on the stirrer, the stirring speed is controlled at 850r / min, and the above-mentioned three kinds of solutions are slowly passed into the reaction kettle at the same time; wherein, the cobalt chloride solution flow rate is controlled at 9ml / min, the ammonia flow rate is controlled at 4.5ml / min, and the hydration The flow rate of hydrazine is controlled at 1.5ml / min; while feeding, the temperature of the mixed s...
Embodiment 3
[0064] 1) prepare cobalt chloride solution, hydrazine hydrate solution and ammoniacal liquor of certain concentration, the molar concentration of cobalt ion in the cobalt chloride solution is 3mol / L, the hydrazine hydrate concentration is 30%, and the ammoniacal liquor concentration is 25%;
[0065] 2) Add 40L of pure water bottom liquid into the 200L reaction kettle, the bottom liquid just covers the blade of the agitator, open the heating steam valve, and heat the temperature in the kettle to 55°C;
[0066] 3) Turn on the stirrer, control the stirring speed at 900r / min, and slowly feed the above three solutions into the reactor simultaneously; wherein, the cobalt chloride solution flow rate is controlled at 106ml / min, the ammonia flow rate is controlled at 21ml / min, and the hydrazine hydrate The flow rate is controlled at 106ml / min; while feeding, the temperature of the mixed solution is controlled at 55±0.5°C, and the pH of the mixed solution is controlled at 11.3±0.1;
[0...
PUM
| Property | Measurement | Unit |
|---|---|---|
| concentration | aaaaa | aaaaa |
| particle size | aaaaa | aaaaa |
| particle size | aaaaa | aaaaa |
Abstract
Description
Claims
Application Information
Login to View More 