Method for ultrasonically leaching valuable elements from high temperature alloy scraps for comprehensive utilization
A technology of superalloy and valuable elements, which is applied in the field of comprehensive utilization of superalloy waste by ultrasonic leaching, can solve the problems of inability to comprehensively recover valuable alloy elements, low alloy dissolution efficiency, equipment corrosion, etc., so as to avoid strong oxidation The effect of using acid, improving leaching efficiency and reducing equipment corrosion
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Embodiment 1
[0035] The method for the comprehensive utilization of superalloy waste in this embodiment is carried out according to the following steps:
[0036] (1) A kind of nickel-based superalloy cutting waste is mixed with hydrochloric acid with a weight concentration of 15% according to the liquid-solid ratio of 10mL:1g, and is sent into the reactor (leaching section), and the reaction time is 2h. After the reaction, solid-liquid separation is obtained to obtain Nickel-cobalt solution and leaching residue I, wherein the leaching rate of nickel reaches 99.32%, and the leaching rate of cobalt reaches 98.67%;
[0037] (2) After the nickel-cobalt solution obtained in step (1) is through cooperative extraction and stripping, the intermediate product of pure nickel-cobalt solution is obtained; the nickel-cobalt hydroxide battery-grade raw material is obtained through controllable coupling co-precipitation technology, and its impurity content is less than 1 wt%.
[0038] (3) The raffinate ...
Embodiment 2
[0043] The method for the comprehensive utilization of superalloy waste in this embodiment is carried out according to the following steps:
[0044] (1) A kind of nickel-based superalloy grinding waste and weight concentration are 10% hydrochloric acid according to liquid-solid 8mL: 1g mix, send in the reactor, reaction time 1h, solid-liquid separation after the reaction, obtain the solution containing nickel and cobalt , wherein the leaching rate of nickel reaches 99.12%, and the leaching rate of cobalt reaches 98.47%;
[0045] (2) From the nickel-cobalt solution in step (1) through collaborative extraction and stripping, the intermediate product of pure nickel-cobalt solution is obtained, and the nickel-cobalt hydroxide battery-grade raw material is obtained through controllable coupling coprecipitation technology, and its impurity content is less than 1wt %.
[0046] (3) The raffinate is returned to the leaching section to realize the recycling of dilute acid, and no waste...
Embodiment 3
[0051] The method for the comprehensive utilization of superalloy waste in this embodiment is carried out according to the following steps:
[0052] (1) A kind of nickel-base superalloy bulk waste material and the dilute sulfuric acid of 2.5mol / L mix according to liquid-solid ratio 8mL:1g, send in the reactor, reaction time 3h, solid-liquid separation after the reaction, obtain nickel-cobalt-containing solution, wherein the leaching rate of nickel reaches 98.32%, and the leaching rate of cobalt reaches 99.14%;
[0053] (2) From the nickel-cobalt solution in step (1) through collaborative extraction and stripping, the intermediate product of pure nickel-cobalt solution is obtained; the nickel-cobalt hydroxide battery-grade raw material is obtained through controllable coupling coprecipitation technology, and its impurity content is less than 1wt %.
[0054] (3) The raffinate is returned to the leaching section to realize the recycling of dilute acid, and no waste acid solution...
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