Method for extracting rubdium and cesium from acid brine

A brine, rubidium-cesium technology, applied in the field of extracting rubidium-cesium, can solve problems such as unreported technical solutions, lack of brine pre-treatment process, great adsorption and separation interference, low production cost, easy solid-liquid separation, The effect of improving extraction efficiency

Inactive Publication Date: 2016-01-20
QINGHAI INST OF SALT LAKES OF CHINESE ACAD OF SCI
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  • Abstract
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  • Application Information

AI Technical Summary

Problems solved by technology

[0005] Although existing patents and periodicals and other documents disclose or report the process route and method of extracting rubidium and cesium by t-BAMBP, they lack the brine pretreatment process, but a large amount of calcium and magnesium ions in the actual brine will affect the extraction process
Moreover, the composition of the actual

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  • Method for extracting rubdium and cesium from acid brine

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Experimental program
Comparison scheme
Effect test

Embodiment 1

[0028] see figure 1 , at 25°C, the initial concentrations of rubidium, cesium, sodium, potassium, calcium, and magnesium ions in brine were 19.0mg / L, 2.0mg / L, 30.55g / L, 20.60g / L, 23.84g / L, and 28.38 g / L, take 50g of ammonium-type chelating resin and pack it into the column, pump 100mL of simulated brine into the adsorption column, and transfer it to the ammonia water pool for transformation after the resin is saturated, wash away the residual ammonia on the surface and reload it into the adsorption column, and wait for After removing calcium and magnesium, add ammonia water to make the pH of the effluent liquid 11, then mix it with 100 mL of 1mol / L t-BAMBP sulfonated kerosene solution and enter the extraction device to vibrate for 10 minutes, after standing for 5 minutes, the oil and water are separated, and the water phase is discharged for subsequent salt extraction treatment. The organic phase enters the stripping device, add 80mL of 2.0mol / L HCl to shake for 10min, let sta...

Embodiment 2

[0030] At 25°C, the initial concentrations of rubidium, cesium, sodium, potassium, calcium, and magnesium ions in brine are 19.0mg / L, 2.0mg / L, 30.55g / L, 20.60g / L, 23.84g / L, and 28.38g, respectively / L, take 50g of ammonium-type chelating resin and pack it into the column, pump 100mL of simulated brine into the adsorption column, transfer it to the ammonia water pool for transformation after the resin is saturated, wash off the residual ammonia on the surface and reload it into the adsorption column, wait for the calcium After removing magnesium, add ammonia water to make the pH of the effluent liquid 11, then mix it with 100 mL of 1mol / L t-BAMBP sulfonated kerosene solution and enter the extraction device to vibrate for 5 minutes. phase into the stripping device, add 80mL of 2.0mol / L HCl to shake for 10min, let stand for 5min to separate oil and water, pump the organic phase into the extraction device for recycling, evaporate and crystallize the water phase on the heating plate...

Embodiment 3

[0032] At 25°C, the initial concentrations of rubidium, cesium, sodium, potassium, calcium, and magnesium ions in brine are 19.0mg / L, 2.0mg / L, 30.55g / L, 20.60g / L, 23.84g / L, and 28.38g, respectively / L, take 50g of ammonium-type chelating resin and pack it into the column, pump 100mL of simulated brine into the adsorption column, transfer it to the ammonia water pool for transformation after the resin is saturated, wash off the residual ammonia on the surface and reload it into the adsorption column, wait for the calcium After removing magnesium, add ammonia water to make the pH of the effluent liquid 11, then mix it with 100 mL of 1mol / L t-BAMBP sulfonated kerosene solution and enter the extraction device to vibrate for 10 minutes, after standing for 5 minutes, the oil and water are separated, and the water phase is discharged for subsequent salt extraction treatment, organic phase into the stripping device, add 80mL of 2.0mol / L HCl to shake for 5min, stand for 5min for oil-wat...

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Abstract

The invention discloses a method for extracting rubdium and cesium from acid brine. The method includes the steps that brine is pumped into an ammonium type chelate resin adsorption column, calcium ions and magnesium ions are adsorbed through the ammonium type chelate resin adsorption column, and effluent is brine without the calcium ions and the magnesium ions; the effluent is mixed with t-BAMBP or kerosene or sulfonated kerosene to be shaken, and a mixture stands still for layering and separation of a water phase and an organic phase; and reextraction is conducted on the organic phase, and the water phase containing rubidium chloride and cesium chloride is obtained. The method is simple in process, low in production cost, capable of achieving separate extraction for removing rubdium and cesium ions in radioactive water and free of secondary pollution.

Description

technical field [0001] The invention belongs to the field of salt lake chemistry and chemical industry, and in particular relates to a method for extracting rubidium and cesium from acid brine. Background technique [0002] Rubidium and cesium are abundant in the earth's crust, ranking 16th and 40th respectively in terms of element abundance. They are mainly abundant in solid ores such as lepidolite and cesium garnet, and in salt lake brine. Rubidium and cesium have strong chemical activity and excellent photoelectric properties, and have been greatly developed in traditional application fields such as electronic devices, catalysts, and special glasses. [0003] In recent years, with the in-depth understanding of rubidium and cesium, rubidium and cesium have also shown strong vitality in emerging application fields such as magnetic fluid power generation, thermionic conversion power generation, and ion propulsion engines. The basic raw materials for the industrial productio...

Claims

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Application Information

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IPC IPC(8): C22B26/10
Inventor 刘海宁胡耀强叶秀深张慧芳吴志坚
Owner QINGHAI INST OF SALT LAKES OF CHINESE ACAD OF SCI
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