Electrorefining of Sodium in Sodium Bis(trifluoromethane)sulfonylimide and Tetrabutylammonium Bis(trifluoromethane)sulfonylimide Mixture Ionic Liquids for Metallic Sodium Recycling

M. Ueda, R. Inaba, H. Matsushima, T. Ohtsuka
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引用次数: 1

Abstract

Metallic sodium is presently used as an intermediate (Sodium Alcoholate) in agricultural chemicals, 1 PCB decomposing agents (Sodium Dispersion), 2,3 and sodium-sulfur secondary batteries. 4,5 Presently, the sodium production has carried out only at a few countries in the world. Therefore, development of a process to circulate metallic sodium is highly desirable not only from resources recycling considerations. A process for electrowinning of sodium (Downs process) 6,7 produces metallic Na and Cl2 gas from NaCl-CaCl2-BaCl2 molten salts. The voltage of the electrolysis increases to exceed the decomposition voltage of NaCl during the electrolysis, and the electrical power consumption is known to be about 11000 kWh/t. In electrorefining to produce highly pure sodium from sodium containing impurities, the decomposition voltage is theoretically zero, and it may be assumed that the electrolysis voltage is not high. As a result it may be expected that the electric power consumption of the electrorefining process becomes less than the electrowinning process. However, no electrorefining process for sodium has been implemented on an industrial scale. In sodium-sulfur batteries where much sodium is contained, a large amount of metallic sodium remains in the batteries also in the used state. The sodium of about 400 kg is used for production of the sodium-sulfur batteries in every year. If metallic sodium is collected fromusedsodium-sulfurbattery, electrorefining ofthe sodiummaybe carried out and resources of high purity sodium could be secured. And we believe that the development of electrorefining process becomes valuable technology in fields of high purity metal production. We have proposed a sodium recycling process which involves collection of the metallic sodium from used sodium-sulfur batteries and refining of the collected metallic sodium. 8‐10 The electrorefining process of the metallic sodium from used Na-S batteries developed by us investigated organic solvents, molten salts, and ionic liquids as the electrolyte. From the results, it was found that an ionic liquid mixture of NaTFSI (sodium bis(trifluoromethane)sulfonylimide) -TBATFSI (tetrabuthylammonium bis (trifluoromethane)sulfonylimide) has a wide electrochemical potential window and that it displays low reactivity with molten metallic sodium below 473 K. This paper reports the melting point of the investigated ionic liquid mixture, its conductance, voltammogram, and the electrorefining reaction with metallic sodium by constant current electrolysis in the NaTFSI-TBATFSI ionic liquid.
电精炼双(三氟甲烷)磺酰亚胺钠和四丁基双(三氟甲烷)磺酰亚胺混合离子液体中钠的金属钠回收
金属钠目前被用作农业化学品、1多氯联苯分解剂(分散钠)、2、3和钠硫二次电池的中间体(酒精钠)。目前,世界上只有少数几个国家进行了钠的生产。因此,开发一种循环金属钠的工艺是非常可取的,不仅从资源回收的考虑。电积钠的工艺(唐斯工艺)6,7从NaCl-CaCl2-BaCl2熔盐中产生金属Na和Cl2气体。电解过程中电解电压升高,超过NaCl的分解电压,已知电耗约为11000kwh /t。电解提纯从含杂质的钠中生产高纯钠时,分解电压理论上为零,可以假定电解电压不高。因此,可以预期电精炼过程的电功率消耗比电积过程要小。然而,钠的电精炼工艺尚未在工业规模上实施。在钠硫电池中,由于含有大量的钠,因此在使用状态下仍有大量的金属钠残留在电池中。每年约有400公斤的钠用于生产钠硫电池。如果从钠硫电池中收集金属钠,可以对钠进行电精制,保证高纯度钠的资源。相信电精炼工艺的发展将成为高纯金属生产领域的一项有价值的技术。我们提出了一种钠回收工艺,包括从废旧钠硫电池中收集金属钠并对收集到的金属钠进行精制。8‐10我们开发的从废Na-S电池中提取金属钠的电精炼工艺研究了有机溶剂、熔盐和离子液体作为电解液。结果表明,NaTFSI(二(三氟甲烷)磺酰亚胺钠)-TBATFSI(四丁基二(三氟甲烷)磺酰亚胺钠)离子液体混合物具有较宽的电化学电位窗口,在473 K以下与熔融金属钠表现出较低的反应活性。本文报道了所研究的离子液体混合物的熔点、电导、伏安,以及在NaTFSI-TBATFSI离子液体中恒流电解与金属钠的电精炼反应。
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ECS Electrochemistry Letters
ECS Electrochemistry Letters ELECTROCHEMISTRY-MATERIALS SCIENCE, MULTIDISCIPLINARY
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