硫化矿\({\text{NH}}_{4}^{ + }\)形态向H+形态的转化

IF 0.6 4区 工程技术 Q4 ENGINEERING, CHEMICAL
E. P. Lokshin, O. A. Tareeva
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引用次数: 0

摘要

研究了硫化矿从\({\text{NH}}_{4}^{ + }\)形态向H+形态的转化过程。结果表明,当使用浓浓无机酸(硝酸、硫酸)溶液时,转化效果不佳。为了实现向H+形式的有效转化,建议分两个阶段处理\({\text{NH}}_{4}^{ + }\)形式的硫化矿:首先用钠盐溶液将其转化为中间的Na+形式,然后用强无机酸溶液获得H+形式的吸附剂。提出了计算达到一定程度的吸附剂转化所需的具体试剂消耗量的公式。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
Conversion of Sulfocationite from \({\text{NH}}_{4}^{ + }\) Form to H+ Form

The conversion of sulfocationite from the \({\text{NH}}_{4}^{ + }\) form to the H+ form is studied. It is shown that when using concentrated solutions of strong mineral acids (nitric, sulfuric), the conversion is ineffective. In order to achieve efficient conversion to the H+ form, it is recommended to treat the sulfocationite in the \({\text{NH}}_{4}^{ + }\) form in two stages: first with a sodium salt solution to convert it to the intermediate Na+ form, then with a strong mineral acid solution to obtain the sorbent in the H+ form. An equation is proposed for calculating the specific reagent consumption required to achieve a certain degree of the sorbent conversion.

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来源期刊
CiteScore
1.20
自引率
25.00%
发文量
70
审稿时长
24 months
期刊介绍: Theoretical Foundations of Chemical Engineering is a comprehensive journal covering all aspects of theoretical and applied research in chemical engineering, including transport phenomena; surface phenomena; processes of mixture separation; theory and methods of chemical reactor design; combined processes and multifunctional reactors; hydromechanic, thermal, diffusion, and chemical processes and apparatus, membrane processes and reactors; biotechnology; dispersed systems; nanotechnologies; process intensification; information modeling and analysis; energy- and resource-saving processes; environmentally clean processes and technologies.
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