Equipment and method for extracting uranium from high-density pulp
A high-density, pulp technology, applied in the field of ion exchange extraction of uranium, can solve the problems of excessive waste water, only 6%, increased water consumption, etc., achieve continuous and automatic reverse flow, solve the retention fraction, and reduce waste water discharge.
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Embodiment 1
[0034] A device for extracting uranium from high-density pulp, the device includes n-stage adsorption units, each stage of adsorption unit includes a mixing chamber and an inter-chamber device, the inter-chamber device of the first-stage adsorption unit and the second-stage adsorption unit The mixing chamber of the second-stage adsorption unit is communicated with the mixing chamber of the third-stage adsorption unit, ..., the inter-chamber device of the n-1st-stage adsorption unit is communicated with the mixing chamber of the n-th-stage adsorption unit;
[0035] It also includes m' stage washing units, each stage washing unit also includes a mixing chamber and an inter-chamber device, the mixing chamber of the 1'-stage adsorption unit is communicated with the inter-chamber device of the 2'-stage adsorption unit, and the 2'-stage adsorption unit The mixing chamber of the unit communicates with the inter-chamber device of the 3'-stage adsorption unit, ..., the mixing chamber of...
Embodiment 2
[0051] Uranium is extracted from a slurry using resin. The density of the leaching pulp solution is 1.5g / L, the uranium content is 1.5g / L, the resin is 201×7 resin, and the wet true density of the resin is 1.10g / cm 3 . The slurry adsorption is carried out using the equipment described in the present invention. The equipment parameters are n=8, m=2, and the side length of the mixing chamber is 300mm. 95% of the pulp was pumped into the first stage adsorption unit of the equipment at a flow rate of 95 L / h. The lean resin was fed into the 8th stage adsorption unit at a rate of 5 L / h. The 5% pulp was filtered to obtain clear liquid, which was pumped into the 2' stage washing unit at a flow rate of 5 L / h. The washing liquid enters the first stage adsorption unit to combine with the pulp in the first stage. In the adsorption unit, the resin enters the mixing chamber from the upper opening, and exits the mixing chamber from the lower opening. The pulp enters the mixing chamber f...
Embodiment 3
[0053] Uranium is extracted from a slurry using resin. The density of the leaching pulp solution is 1.3g / L, the uranium content is 1.25g / L, the resin is 201×7 resin, and the wet true density of the resin is 1.10g / cm 3 . The slurry adsorption is carried out using the equipment described in the present invention. The equipment parameters are n=10, m=4, and the side length of the mixing chamber is 500 mm. 90% of the pulp was pumped into the first stage adsorption unit of the equipment at a flow rate of 450 L / h. Lean resin was fed to the 10th stage adsorption unit at a rate of 25 L / h. The clear liquid obtained by filtration of 10% of the pulp was pumped into the 2' stage washing unit at a flow rate of 10L / h. The washing liquid enters the first stage adsorption unit to combine with the pulp in the first stage. In the adsorption unit, the resin enters the mixing chamber from the upper opening, and exits the mixing chamber from the lower opening. The pulp enters the mixing chamb...
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