Method for recovering rare earth in neodymium-iron-boron waste by high-temperature and high-pressure leaching
A technology for recycling NdFeB, high temperature and high pressure, applied in the direction of improving process efficiency, etc., can solve the problems of high waste particle size requirements, low hydrochloric acid utilization rate, long leaching time, etc., to achieve increased hydrochloric acid utilization rate, low hydrochloric acid consumption, and improved The effect of recovery value
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Embodiment 1
[0049] This embodiment provides a method for high temperature and high pressure leaching and recovery of rare earths in NdFeB waste, comprising the following steps:
[0050] S1: Take 300g of NdFeB waste powder, particle size -100 mesh, chemical composition (mass percentage): TRE-29.14, Fe-66.34, Co-0.74, Al-0.38, B-0.96. The above-mentioned NdFeB waste is oxidized and roasted so that the content of low-valent iron oxide FeO in it is less than 1%, and then crushed and ground to below -100 mesh.
[0051] S2: Get 30.00 g of waste powder after roasting, 23.19 g of 37% concentrated hydrochloric acid is diluted with water to 90 g (the amount of HCl is 1.15 times of the theoretical amount), and the mixed material liquid composed of the two is added into the autoclave, and the autoclave is sealed. The pressure in the autoclave is 0.6MPa, the leaching temperature is 110°C, the stirring speed is 300r / min, and the leaching time is 30min. After the leaching is completed, take out the auto...
Embodiment 2
[0055] This embodiment provides a method for high temperature and high pressure leaching and recovery of rare earths in NdFeB waste, comprising the following steps:
[0056] S1: Select the NdFeB waste powder obtained by roasting in Example 1, further crush and grind to a particle size of -200 mesh.
[0057] S2: Take 30.00g of roasted NdFeB waste powder, add 23.19g of 37% concentrated hydrochloric acid and dilute it to 90g with water (the amount of HCl is 1.15 times the theoretical amount), add the mixed material liquid formed by the two into the autoclave, seal Autoclave, the pressure inside the autoclave is 0.6MPa, the leaching temperature is 110°C, the stirring speed is 300r / min, and the leaching time is 30min. After the leaching is completed, the reactor is taken out, and the solid and liquid are separated to obtain the leachate.
[0058] S3: Slowly add oxidant H to the leaching solution under stirring 2 o 2 15mL, so that the Fe 2+ fully oxidized.
[0059] S4: neutrali...
Embodiment 3
[0061] This embodiment provides a method for high temperature and high pressure leaching and recovery of rare earths in NdFeB waste, comprising the following steps:
[0062] S1: select the NdFeB waste powder obtained by roasting in Example 1.
[0063] S2: Get 30.00g of NdFeB waste powder after roasting, add 25.61g of 37% concentrated hydrochloric acid and dilute to 90g with water (the amount of HCl is 1.27 times of the theoretical amount), add the mixed material liquid formed by the two into the autoclave, Seal the autoclave so that the pressure inside the autoclave is 1.0MPa, the leaching temperature is 110°C, the stirring speed is 300r / min, and the leaching time is 30min. After the leaching is completed, take out the autoclave, separate the solid and liquid, and obtain the leachate.
[0064] S3: Leave the leaching solution open for 24 hours, using air as the oxidant to oxidize the Fe in it 2+ , and slowly add the oxidant H to the leaching solution under stirring 2 o 2 5m...
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