A method for efficient selective adsorption recovery of rhenium and mercury from multi-component mixed waste acid of copper smelting
A technology of selective adsorption and copper smelting, applied in the direction of improving process efficiency, etc., can solve the problems of difficult production of ammonium rhenate, pollution of rhenium-rich liquid, high toxicity of mercury, etc., and achieve the effects of low cost, easy industrialization, and short process
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Embodiment 1
[0066] Step 1. Resin pretreatment
[0067] Measure 80ml of D304 type anion exchange resin, pour it into a 200ml beaker, add 80ml of circulating water of copper smelting enterprise, 80ml of tap water respectively, soak and swell at room temperature statically for 15h, pour off the swelling water after swelling, and use circulating water and tap water with a volume ratio of 1 Washing with mixed water of 1:1 to pH=7, adding 200ml of mixed alkali of KOH and ammonia water, wherein the mass concentration of KOH is 0.2%, the concentration of ammonia water is 0.1%, the alkali immersion transformation is 2h, and the resin is washed to pH with circulating water after the transformation is completed = 7.5, use a copper smelting multi-component mixed waste acid in Northwest China to carry out acid leaching transformation for 24 hours, after the transformation is completed, it will not be washed with water, and it will be used directly.
[0068] Step 2. Pretreatment of multiple mixed waste...
Embodiment 2
[0077] Step 1. Resin pretreatment
[0078] Measure 50ml of D304 type anion exchange resin, pour it into a 200ml beaker, add 50ml of tap water and 50ml of demineralized water respectively, soak and swell at room temperature statically for 10 hours, pour off the swelling water after the swelling is completed, wash the resin with tap water until pH = 7, add NaOH and Mixed alkali 100ml of ammonia water, wherein the mass concentration of NaOH is 2.5%, the concentration of ammonia water is 0.5%, the alkali leaching transformation is 5h, after the transformation is completed, the resin is washed to pH=9.0 with tap water, and the mixed acid of 2.5% sulfuric acid and hydrofluoric acid is used (The mass ratio of sulfuric acid and hydrofluoric acid is 9:1) acid leaching transformation for 8 hours, after the transformation, wash with tap water to pH = 5 and set aside.
[0079] Step 2. Pretreatment of multiple mixed waste acids
[0080] Take SO from a copper smelter in Central China 2 Se...
Embodiment 3
[0088] Step 1. Resin pretreatment
[0089] Measure 40ml of D304 anion exchange resin, pour it into a 200ml beaker, add 100ml of demineralized water, soak and swell for 30 hours at room temperature, pour off the swelling water after the swelling is completed, wash the resin with demineralized water until pH = 7, add 8% ammonia water 60ml for alkali Immersion transition 10h, after the transformation is over, use demineralized water to wash the resin to pH=8.5, adopt 3.0% sulfuric acid and hydrochloric acid mixed acid (the mass ratio of sulfuric acid and hydrochloric acid is 9:1) acid leaching transformation for 30h, and the transformation ends and demineralized water washing to pH = 4 and ready to use.
[0090] Step 2. Pretreatment of multiple mixed waste acids
[0091] Take SO from a copper smelter in Southwest China 2 Secondary power wave cooling and purification of 25L of dirty acid, adding amphoteric polyacrylamide flocculant at a rate of one ten thousandth, settling for 2...
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