Novel method and device for recovering metal palladium
A kind of metal palladium, the technology of the new method is applied in the field of recovering metal palladium, the method and the special device, and achieves the effect of multiple economic benefits
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Embodiment 1
[0026] Such as figure 1 Shown, the device that a kind of new method that the present invention reclaims metallic palladium adopts, comprises the waste liquid tank 1 that is connected successively, reaction tank 2, sedimentation filter tank 3, delivery pump 4, electrolyzer 5; Reaction tank 2 and hydroxyl free radical The generator 6 is connected, and the precipitation filter tank 3 is connected with the alkali solution tank 7 and the acid solution tank 8 respectively.
[0027] Wherein, the reaction tank 2 is provided with a first waste liquid inlet and an oxidant dosing port; the sedimentation filter tank 3 is provided with a second waste liquid inlet, an lye dosing port and an acid liquid dosing port; A third waste liquid inlet and a waste liquid discharge port are arranged on it; a stirrer 9 is arranged in the reaction pool 2 .
Embodiment 2
[0029] A kind of new method of reclaiming metal palladium adopts the device of embodiment 1 to process, specifically comprises the steps:
[0030] (A) the waste liquid containing colloidal palladium of circuit board production line is sent into waste liquid tank 1 and concentrates;
[0031] (B) Send the waste liquid of waste liquid tank 1 into reaction tank 2, adopt hydroxyl radical generator 6 to add oxidizing agent online, carry out oxidation reaction under stirring, destroy the particle structure of colloidal palladium, make it form ion palladium and ion Tin; the oxidizing agent is hydroxyl radical, the dosage is 21g / t waste liquid, and the reaction stirring time after adding hydroxyl radical is 2 hours.
[0032] (C) Send the waste liquid from the reaction tank 2 into the sedimentation filter tank 3, add 10% lye online, control the pH value of the waste liquid ≥ 8, realize almost complete precipitation of the ionic tin, and remove the ionic tin by filtering and separating; ...
Embodiment 3
[0036] The difference from Example 2 is: the dosage of hydroxyl radicals in step (B) is 22 g / t waste liquid, and the reaction stirring time after adding hydroxyl radicals is 1.9 hours. Others are identical with embodiment 2.
[0037] After electrolysis, the waste liquid was sampled and tested: the recovery rate of palladium was 94.5%.
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