无机盐工业
主管:中海油天津化工研究设计院有限公司
主办:中海油天津化工研究设计院有限公司
   中海油炼油化工科学研究院(北京)有限公司
   中国化工学会无机酸碱盐专业委员会
ISSN 1006-4990 CN 12-1069/TQ

无机盐工业 ›› 2025, Vol. 57 ›› Issue (9): 61-65.doi: 10.19964/j.issn.1006-4990.2024-0485

• 研究与开发 • 上一篇    下一篇

察尔汗盐湖老卤合成碱式碳酸镁实验研究

孙泽妍1(), 张乐2, 何佳颖2, 谷双双2, 甘顺鹏1   

  1. 1.中蓝长化工程科技有限公司,湖南 长沙 410116
    2.青海盐湖工业股份有限公司,青海格尔木 816000
  • 收稿日期:2024-09-02 出版日期:2025-09-10 发布日期:2024-11-25
  • 作者简介:孙泽妍(1992— ),女,硕士,工程师,主要研究方向为卤水资源化利用;E-mail:szy_326@163.com

Experimental study on Qarhan Salt Lake old brine for production of magnesium carbonate hydromagnesite

SUN Zeyan1(), ZHANG Le2, HE Jiaying2, GU Shuangshuang2, GAN Shunpeng1   

  1. 1. Zhonglan Changhua Engineering Technology Co. ,Ltd. ,Changsha 410116,China
    2. Qinghai Salt Lake Industrial Co. ,Ltd. ,Golmud 816000,China
  • Received:2024-09-02 Published:2025-09-10 Online:2024-11-25

摘要:

针对察尔汗盐湖老卤生产碱式碳酸镁过程中所得滤饼中氯含量高导致生产所需用水量大的问题,提出一种利用察尔汗盐湖老卤两步法制备碱式碳酸镁的新思路。重点探究了一步法与两步法在制备碱式碳酸镁过程中用水量及氯含量的差异,并通过XRD、SEM等表征技术对样品的晶型、形貌进行了表征,揭示了反应过程的机理。结果表明:利用两步法合成工艺过程中,首先通过制备棒状结构的三水碳酸镁,不仅可提升过滤效率且极大降低了滤饼中氯离子的夹带率,相比一步法合成工艺,在未使用淋洗液的条件下,所得固样中氯离子夹带含量由6.12%下降至2.16%(质量分数),同时生产所需用水量仅为一步法所需生产用水量的40%,最终所得产品中MgO含量、Cl⁻含量满足HG/T 2959—2023《工业水合碱式碳酸镁》,且最终收率可达97.06%。因此,利用两步法合成碱式碳酸镁可明显改善一步法工艺大量用水问题,同时此工艺可为察尔汗盐湖老卤制备碱式碳酸镁工艺提供重要参考。

关键词: 察尔汗盐湖老卤, 碱式碳酸镁, 三水碳酸镁, 纯碱法

Abstract:

In order to solve the problem of high chlorine content in filter cake during the production of basic magnesium carbonate from the old brine of Qarhan Salt Lake,a new idea of using the old brine of Qarhan Salt Lake to prepare basic magnesium carbonate was put forward.The differences of water consumption and chlorine content between one-step method and two-step method in the preparation of basic magnesium carbonate were studied,and the crystal shape and morphology of the samples were characterized by XRD,SEM and other characterization techniques,and the mechanism of the reaction process was revealed.The test results showed that in the two-step synthesis process,the rod-like magnesium carbonate trihydrate was prepared firstly,which not only improved the filtration efficiency but also greatly reduced the chloride ion entraining rate in the filter cake.Compared with the one-step synthesis process,the chloride ion entraining content in the obtained solid sample was reduced from 6.12% to 2.16%(mass fraction) without using the leach solution.At the same time,the water consumption of the production was only 40% that of the one-step process.The content of MgO and Cl⁻ in the final product met the HG/T 2959—2023 standard of "Industrial hydrated basic magnesium carbonate" and the final yield could reach 97.06%.Therefore,the use of two-step synthesis of basic magnesium carbonate could obviously improve the problem of a large amount of water in the one-step process,and this process could provide an important reference for the preparation of basic magnesium carbonate from the old brine of Qarhan Salt Lake.

Key words: old brine from Qarhan Salt Lake, basic magnesium carbonate, magnesium carbonate trihydrate, soda ash process

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