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An Environmentally Friendly Process Involving Refining and Membrane-Based Electrolysis for Magnesium Recovery from Partially Oxidized Scrap Alloy

机译:涉及精炼和基于膜的电解从部分氧化废合金中回收镁的环保工艺

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摘要

Magnesium is recovered from partially oxidized scrap alloy by combining refining and solid oxide membrane (SOM) electrolysis. In this combined pro cess, a molten salt eutectic flux (45 wt.% MgF_2-55 wt.% CaF_2) containing 10 wt.% MgO and 2 wt.% YF_3 was used as the medium for magnesium recovery. During refining, magnesium and its oxide are dissolved from the scrap into the molten flux. Forming gas is bubbled through the flux and the dissolved magnesium is removed via the gas phase and condensed in a sepa rate condenser at a lower temperature. The molten flux has a finite solubility for magnesium and acts as a selective medium for magnesium dissolution, but not aluminum or iron, and therefore the magnesium recovered has high purity. After refining, SOM electrolysis is performed in the same reactor to enable electrolysis of the dissolved magnesium oxide in the molten flux pro ducing magnesium at the cathode and oxygen at the SOM anode. During SOM electrolysis, it is necessary to decrease the concentration of the dissolved magnesium in the flux to improve the faradaic current efficiency and prevent degradation of the SOM. Thus, for both refining and SOM electrolysis, it is very important to measure and control the magnesium solubility in the molten flux. High magnesium solubility facilitates refining whereas lower solubility benefits the SOM electrolysis process. Computational fluid dynamics modeling was employed to simulate the flow behavior of the flux stirred by the forming gas. Based on the modeling results, an optimized design of the stirring tubes and its placement in the flux are determined for efficiently removing the dissolved magnesium and also increasing the efficiency of the SOM electrol ysis process.
机译:通过将精炼和固体氧化物膜(SOM)电解相结合,从部分氧化的废合金中回收镁。在该组合过程中,将包含10重量%的MgO和2重量%的YF_3的熔融盐共晶熔剂(45重量%的MgF_2-55重量%的CaF_2)用作镁回收的介质。在精炼过程中,镁及其氧化物从废料中溶解到熔融熔剂中。使形成的气体鼓泡通过助熔剂,并通过气相除去溶解的镁,并在较低温度的分离器冷凝器中冷凝。熔融的熔剂对镁具有有限的溶解度,并且充当镁溶解的选择性介质,而不是铝或铁,因此回收的镁具有高纯度。精制后,在同一反应器中进行SOM电解,以使熔融助熔剂中溶解的氧化镁电解,从而在阴极生成镁,在SOM阳极生成氧气。在SOM电解过程中,有必要降低焊剂中溶解的镁的浓度,以提高法拉第电流效率并防止SOM降解。因此,对于精炼和SOM电解,测量和控制镁在熔剂中的溶解度非常重要。高镁溶解度有助于提纯,而低溶解度则有利于SOM电解过程。计算流体动力学模型被用来模拟由形成气体搅拌的助熔剂的流动行为。根据建模结果,可以确定搅拌管的优化设计及其在焊剂中的位置,以有效去除溶解的镁并提高SOM电解过程的效率。

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