Biological leaching-aluminum carbon micro-electrolysis treatment of aluminum profile electroplating waste slag equipment reactor
A technology of aluminum carbon micro-electrolysis and electroplating waste residue, which is applied in the field of resources and environment to achieve the effect of increasing mass transfer efficiency
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Embodiment 1
[0031] Example 1 A biological leaching-aluminum carbon micro-electrolysis treatment of aluminum profile electroplating waste residue equipment reactor
[0032] A biological leaching-aluminum carbon micro-electrolysis equipment reactor for aluminum profile electroplating waste residue, the reactor consists of three parts: a feed storage tank, a reactor and a rich liquid storage tank, and the feed storage tank is connected to the reaction tank through a peristaltic pump 8 One side of the reactor is connected, and the enriched liquid storage tank is connected with the other side of the reactor. The reactor is formed by an outer cylinder 1 and an inner cylinder 2 to form an internal circulation reaction zone. The bottom of the outer cylinder 1 A mud discharge port 3 is provided, and a water inlet pipe 4 and an outlet pipe 5 are respectively arranged on both sides of the outer cylinder body 1. The water inlet pipe 4 communicates with the peristaltic pump 8, and the outlet pipe 5 com...
Embodiment 2
[0037] Example 2 A biological leaching-aluminum carbon micro-electrolysis treatment of aluminum profile electroplating waste slag equipment reactor
[0038] The basic structure of the bioleaching-aluminum-carbon micro-electrolysis treatment of aluminum profile electroplating waste residue equipment reactor is the same as in Example 1, the difference is that the reactor includes two sets of porous carbon plates, two sets of aeration discs, and an outer cylinder The height-to-diameter ratio H / D of the body 1 is 2.5, the maximum effective volume ratio η is 75%, the inner diameter D of the outer cylinder 1 / the inner diameter d of the inner cylinder 2 is 2.0, and the difference between the height H of the outer cylinder 1 and the height h of the inner cylinder 2 It is 15cm. The bottom of the outer cylinder 1 is a cone, the angle β between the cone and the horizontal plane is 60°, the inner diameter ψ2 of the bottom of the cone is 0.5D, and the bottom of the cone is provided with a ...
Embodiment 3
[0040] The basic structure of the bioleaching-aluminum-carbon micro-electrolysis treatment of aluminum profile electroplating waste slag equipment reactor is the same as in Example 1, the difference is that the reactor includes three sets of porous carbon plates, three sets of aeration discs, and an outer cylinder The height-to-diameter ratio H / D of the body 1 is 2.2, the maximum effective volume ratio η is 73%, the inner diameter D of the outer cylinder 1 / the inner diameter d of the inner cylinder 2 is 1.7, and the difference between the height H of the outer cylinder 1 and the height h of the inner cylinder 2 It is 13cm. The bottom of the outer cylinder 1 is a cone, the angle β between the cone and the horizontal plane is 55°, the inner diameter ψ2 of the bottom of the cone is 0.5D, and the bottom of the cone is provided with a mud discharge port with a diameter of 4.0cm. The bottom is 50cm from the ground. The upper part of the inner cylinder 2 is provided with an expansio...
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