Method for enriching rare earth from rare earth leaching mother liquor
A rare earth and leaching technology, which is applied in the direction of improving process efficiency, can solve the problems of low amount of rare earth adsorbed by resin and low effective utilization rate of extractant, etc., and achieve the effect of convenient operation and simple process
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[0033] (1) Preparation of mixed resin:
[0034] A mixed resin prepared by mechanically mixing a single phosphorus extractant resin and a single amine extractant resin at a mass ratio of 1:0.1~5; or a composition of a phosphorus extractant and an amine extractant at a mass ratio of 1:0.1~5 The mixed resin prepared by the mixed extractant;
[0035] (2) Column packing:
[0036] The activated carbon adsorption material obtained in step (1) is loaded into an ion exchange column with a column diameter of 1 to 300 cm and a height-to-diameter ratio of 1 to 80:1 by a wet column packing method;
[0037] (3) Column enrichment:
[0038] The ion-exchange column that step (2) packs obtains carries out multi-column series connection to obtain separation column, and the series connection method is as follows figure 2 ; The separation column is divided into extraction column F and back extraction column H according to the column connection section, and the direction of the column is along t...
Embodiment 1
[0044] Weigh dry 2-ethylhexyl phosphate mono-2-ethylhexyl ester (P507) resin and trialkyl tertiary amine (N235) resin in a mass ratio of 1:1 and mix evenly to form a mixed resin, add distilled water to completely soak the resin , and then packed into an ion-exchange column with a column diameter of 20mm and a column height of 1000mm by the wet column packing method, and the column packing height was 850mm.
[0045] Enrichment process route such as figure 1 , multi-column series such as figure 2 . The process includes 10 separation columns, including 5 extraction columns and 5 stripping columns. Leach the mother liquor with a rare earth pH value of 4.0 at 1.5cm·min -1 The flow rate from F 1 Flow through the separation column at 0.5cm·min with hydrochloric acid with a concentration of 5.5mol / L -1 The flow rate from H 1 Flow through the separation column at F 1 After column adsorption saturation, F 1 The column moves into the stripping section. in H 4 The rare earth en...
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