Method for extracting rubidium salt and cesium salt

A technology for cesium salts and rubidium salts, which is applied in the field of extracting rubidium salts and cesium salts, can solve the problems that industrialization and semi-industrialization are far away, complicated in steps, waste of manpower, material resources, financial resources, time, etc. The extraction method is simple and the effect of good application prospects

Active Publication Date: 2014-05-14
QINGHAI INST OF SALT LAKES OF CHINESE ACAD OF SCI
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Chinese patent CN86101311A discloses a patent titled "Technical Scheme for Extracting Rubidium and Cesium from Weathering Crust of Acid-Alkaline Magmatic Rock or Ion-Exchange Rare Earth Ore". The extraction agent used is highly toxic and has poor selectivity, which limits its application and development to a large extent.
Most of the existing technologies are optimized for the extraction agent and extraction conditions. The test is carried out in a separatory funnel, and the oil-water two-phase layering is completely carried out under the action of gravity. The time is extremely long; and the extraction process often needs to be used in multiple stages, and the steps required to use the separatory funnel to achieve this purpose are very complicated, resulting in a lot of waste of manpower, material resources, financial resources, and time
There are few studies on the use of extraction equipment in the existing technology, and it is still far away from realizing the industrialization and semi-industrialization of rubidium salt and cesium salt extraction.

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0032] Adjust the pH of high-salinity solutions with sodium, potassium, rubidium, and cesium ions of 120g / L, 60g / L, 10g / L, and 1g / L to 12, and use t-BAMBP (t- The ratio of BAMBP and sulfonated kerosene is 1:3) to extract the alkalized raw material solution, the flow ratio of the organic phase to the aqueous phase is 3:1, the contact time of the two phases is controlled to be 5min, and the countercurrent series is 3 to obtain the loaded rubidium , the organic phase of cesium ions and the raffinate aqueous phase; the loaded organic phase is washed with 0.01mol / L sulfuric acid solution in countercurrent 5 stages, respectively using 0.5mol / L and 2mol / L sulfuric acid, the organic phase and the aqueous phase flow ratio Carry out 2-stage back extraction for 60:1, obtain 296g / L rubidium sulfate solution and 26.5g / L cesium sulfate solution, the blank organic phase is recycled.

Embodiment 2

[0034] Adjust the pH of high-salinity solutions with sodium, potassium, rubidium, and cesium ions of 90g / L, 10g / L, 25g / L, and 25g / L to 13, and use t-BAMBP (t- The ratio of BAMBP and sulfonated kerosene is 1:1) to extract the alkalized raw material solution, the flow ratio of the organic phase to the aqueous phase is 2:1, the contact time of the two phases is controlled to be 10min, and the countercurrent series is 4 to obtain the loaded rubidium , the organic phase of cesium ions and the raffinate aqueous phase; the loaded organic phase is washed with 0.01mol / L hydrochloric acid solution in countercurrent three stages, and the contents of rubidium chloride, potassium chloride and sodium chloride are respectively 325g / L, 1.8 g / L and 0.7g / L stripping solution, the yield of rubidium chloride was 96.2%, and the purity was 99.2%; further, 2mol / L hydrochloric acid was used, and the flow ratio of organic phase to aqueous phase was 20:1 for two-stage reaction Extraction, to obtain rub...

Embodiment 3

[0036] Adjust the pH of high-salinity media with sodium, potassium, rubidium, and cesium ions at 50g / L, 50g / L, 50g / L, and 50g / L to 13, and use t-BAMBP (t- The ratio of BAMBP and sulfonated kerosene is 1:1) to extract the alkalized raw material liquid, the flow ratio of the organic phase to the aqueous phase is 4:1, the contact time of the two phases is controlled to be 0.5min, and the countercurrent series is 5, and the load The organic phase of rubidium and cesium ions and the raffinate aqueous phase; the loaded organic phase is washed with 0.02mol / L sodium hydroxide solution and water respectively in countercurrent 8 stages, and the organic phase is washed with 1mol / L and 4mol / L nitric acid respectively. The 3-stage back-extraction was carried out at a ratio of 10:1 to the aqueous phase to obtain a 190g / L rubidium nitrate solution and a 169g / L cesium nitrate solution, and the blank organic phase was recycled.

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PUM

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Abstract

The invention relates to a method for extracting rubidium salt and cesium salt. The method comprises the steps of 1) regulating a high-salinity solution to obtain an alkaline solution which has a pH value of 11-14; 2) extracting rubidium ions and cesium ions from the alkaline solution obtained from the step 1) in a centrifugal extractor through an organic extracting agent, thus obtaining a loaded organic phase (I) and raffinate; 3) washing the organic phase (I) obtained from the step 2) through washing water to obtain an organic phase (II) and a washing solution; 4) implementing reverse extraction to the loaded organic phase (II) through reverse extraction acid (I) to obtain a rubidium salt reverse extraction solution and an organic phase loaded with cesium ion; and 5) implementing reverse extraction to the organic phase loaded with the cesium salt obtained from the step 4) through reverse extraction acid (II) to obtain a cesium salt reverse extraction solution and a blank organic phase. The extraction method disclosed by the invention is simple and easy to implement, and can be matched with comprehensive development and utilization of a high-salinity medium to produce a rubidium salt and cesium salt product of preset type.

Description

technical field [0001] The invention relates to the field of hydrometallurgy, in particular to a method for extracting rubidium salt and cesium salt. Background technique [0002] Rubidium and cesium are two kinds of rare elements with extremely active chemical properties, which have excellent photoelectric properties, and have important uses in the fields of catalysts, photovoltaic cells, magnetic fluid power generation, and medicine. The content of rubidium in seawater is 0.15 mg / L. To extract 1 ton of rubidium from seawater, it needs to process 6 million cubic meters of seawater. However, the content of rubidium and cesium in high-salinity solutions such as some salt mine brines in Qinghai, Sichuan and other places and Jiangxi Yichun lepidolite lithium extraction mother liquor are 45-120 mg / L and 2-100 mg / L, which are dozens of times that in seawater. The concentration of other salt products can reach several grams / liter or tens of grams / liter during the production proce...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C01D17/00B01D11/04C22B3/26C22B26/10
CPCY02P10/20
Inventor 高丹丹魏明边绍菊刘鑫党力董亚萍李武
Owner QINGHAI INST OF SALT LAKES OF CHINESE ACAD OF SCI
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