A novel method to recover NaCl from molten salt chlorination residue and recycle NaCl back into molten salt chlorination process in TiCl4 production: Based on phase diagrams analysis
{"title":"A novel method to recover NaCl from molten salt chlorination residue and recycle NaCl back into molten salt chlorination process in TiCl4 production: Based on phase diagrams analysis","authors":"Yufeng Guo, Yu Zheng, Feng Chen, Shuai Wang, Lingzhi Yang, Hao Li","doi":"10.1016/j.psep.2025.107024","DOIUrl":null,"url":null,"abstract":"<div><div>TiCl<sub>4</sub> is the significant intermediate to produce high-end titanium materials. Molten salt chlorination is the main way to produce TiCl<sub>4</sub> in China. However, there is a large amount of molten salt chlorination residue (MSCR) produced during this process. The complex residue is difficult to be treated, causing serious environmental problems. To reduce environmental pollution associated with MSCR and recycle NaCl in the molten salt chlorination process, a novel process of phase transition to recover gaseous NaCl from MSCR was proposed. CaCl<sub>2</sub> and MgCl<sub>2</sub> are the dominant impurities to hinder the recovery of NaCl. Thus, the influence mechanism of CaCl<sub>2</sub> and MgCl<sub>2</sub> and improvements in the recovery of NaCl were systematically investigated in this work, including the thermodynamic phase diagrams analyses, the effects of additive of Na<sub>2</sub>SiO<sub>3</sub> and temperature. As a result, sodium magnesium silicate and sodium calcium silicate were prohibited to generate and the recovery efficiency of NaCl was promoted along with the increasing activity of NaCl. The recovery efficiency of NaCl is 94.36 % and the content of NaCl in the gaseous product is 99.96 % at 1200℃ when n(CaCl<sub>2</sub>+MgCl<sub>2</sub>): n(Na<sub>2</sub>SiO<sub>3</sub>) = 1:1. This method successfully realizes the harmless treatment of MSCR and the recovery of sodium chloride.</div></div>","PeriodicalId":20743,"journal":{"name":"Process Safety and Environmental Protection","volume":"197 ","pages":"Article 107024"},"PeriodicalIF":6.9000,"publicationDate":"2025-03-13","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":"0","resultStr":null,"platform":"Semanticscholar","paperid":null,"PeriodicalName":"Process Safety and Environmental Protection","FirstCategoryId":"93","ListUrlMain":"https://www.sciencedirect.com/science/article/pii/S0957582025002915","RegionNum":2,"RegionCategory":"环境科学与生态学","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":null,"EPubDate":"","PubModel":"","JCR":"Q1","JCRName":"ENGINEERING, CHEMICAL","Score":null,"Total":0}
引用次数: 0
Abstract
TiCl4 is the significant intermediate to produce high-end titanium materials. Molten salt chlorination is the main way to produce TiCl4 in China. However, there is a large amount of molten salt chlorination residue (MSCR) produced during this process. The complex residue is difficult to be treated, causing serious environmental problems. To reduce environmental pollution associated with MSCR and recycle NaCl in the molten salt chlorination process, a novel process of phase transition to recover gaseous NaCl from MSCR was proposed. CaCl2 and MgCl2 are the dominant impurities to hinder the recovery of NaCl. Thus, the influence mechanism of CaCl2 and MgCl2 and improvements in the recovery of NaCl were systematically investigated in this work, including the thermodynamic phase diagrams analyses, the effects of additive of Na2SiO3 and temperature. As a result, sodium magnesium silicate and sodium calcium silicate were prohibited to generate and the recovery efficiency of NaCl was promoted along with the increasing activity of NaCl. The recovery efficiency of NaCl is 94.36 % and the content of NaCl in the gaseous product is 99.96 % at 1200℃ when n(CaCl2+MgCl2): n(Na2SiO3) = 1:1. This method successfully realizes the harmless treatment of MSCR and the recovery of sodium chloride.
期刊介绍:
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