• 文献检索
  • 文档翻译
  • 深度研究
  • 学术资讯
  • Suppr Zotero 插件Zotero 插件
  • 邀请有礼
  • 套餐&价格
  • 历史记录
应用&插件
Suppr Zotero 插件Zotero 插件浏览器插件Mac 客户端Windows 客户端微信小程序
定价
高级版会员购买积分包购买API积分包
服务
文献检索文档翻译深度研究API 文档MCP 服务
关于我们
关于 Suppr公司介绍联系我们用户协议隐私条款
关注我们

Suppr 超能文献

核心技术专利:CN118964589B侵权必究
粤ICP备2023148730 号-1Suppr @ 2026

文献检索

告别复杂PubMed语法,用中文像聊天一样搜索,搜遍4000万医学文献。AI智能推荐,让科研检索更轻松。

立即免费搜索

文件翻译

保留排版,准确专业,支持PDF/Word/PPT等文件格式,支持 12+语言互译。

免费翻译文档

深度研究

AI帮你快速写综述,25分钟生成高质量综述,智能提取关键信息,辅助科研写作。

立即免费体验

使用Aliquat 336从水溶液中进行锗的非分散萃取的数学建模

Mathematical modeling on non-dispersive extraction of germanium from aqueous solutions using Aliquat 336.

作者信息

Kamran Haghighi Hossein, Irannajad Mehdi, Fortuny Agustin, Sastre Ana Maria

机构信息

Department of Mining and Metallurgy, Amirkabir University of Technology, Tehran, Iran E-mail:

Department of Chemical Engineering, Universitat Politècnica de Catalunya, EPSEVG, Av. Víctor Balaguer s/n, 08800 Vilanova i la Geltrú, Spain.

出版信息

Water Sci Technol. 2018 Dec;78(12):2489-2499. doi: 10.2166/wst.2019.002.

DOI:10.2166/wst.2019.002
PMID:30767914
Abstract

In this work, the mathematical modeling of the facilitated transport of germanium (non-dispersive extraction) through a flat sheet membrane with an Aliquat 336 carrier was described. The flat sheet supported liquid membrane (FSSLM) experiments were performed under conditions germanium ≈ 100 mg/L, tartaric acid concentration of 2.76 mmol/L, and carrier concentrations of 2.5-10%v/v. The extraction equilibrium, mass transfer, and diffusion equations based on Fick's law were the principles of modeling. Modeling was carried out by programming in Matlab mathematical software to obtain the extraction (K) and mass transfer constants (K) as the objective parameters. According to the model resolution, K and K were found to be 0.178 and 9.25 × 10 cm/s, respectively. The correlation coefficients between model and experimental data relating to the Aliquat 336 concentrations of 2.5, 5, 7.5, and 10%v/v were found as 0.96, 0.98, 0.99, and 0.92. The parameters of root mean square error, bias, and scatter index showed the model accuracy. In addition, diffusion coefficients relating to Aliquat 336 concentrations of 2.5, 5, 7.5, and 10%v/v were calculated using mass transfer coefficients to be 2.4 × 10, 2.23 × 10, 1.91 × 10, and 1.79 × 10 cm/s, respectively.

摘要

在本研究中,描述了用Aliquat 336载体通过平板膜促进锗传输(非分散萃取)的数学模型。平板支撑液膜(FSSLM)实验是在锗浓度约为100mg/L、酒石酸浓度为2.76mmol/L以及载体浓度为2.5 - 10%v/v的条件下进行的。基于菲克定律的萃取平衡、传质和扩散方程是建模的原理。通过在Matlab数学软件中编程进行建模,以获得萃取常数(K)和传质常数(K)作为目标参数。根据模型解析,发现K和K分别为0.178和9.25×10 cm/s。与2.5%v/v、5%v/v、7.5%v/v和10%v/v的Aliquat 336浓度相关的模型与实验数据之间的相关系数分别为0.96、0.98、0.99和0.92。均方根误差、偏差和散射指数参数显示了模型的准确性。此外,利用传质系数计算得到与2.5%v/v、5%v/v、7.5%v/v和10%v/v的Aliquat 336浓度相关的扩散系数分别为2.4×10、2.23×10、1.91×10和1.79×10 cm/s。

相似文献

1
Mathematical modeling on non-dispersive extraction of germanium from aqueous solutions using Aliquat 336.使用Aliquat 336从水溶液中进行锗的非分散萃取的数学建模
Water Sci Technol. 2018 Dec;78(12):2489-2499. doi: 10.2166/wst.2019.002.
2
Indium extraction from nitrate medium using Cyphos ionic liquid 104 and its mathematical modeling.用 Cyphos 离子液体 104 从硝酸盐介质中提取铟及其数学建模。
Environ Sci Pollut Res Int. 2023 Oct;30(49):107341-107349. doi: 10.1007/s11356-022-24936-z. Epub 2022 Dec 27.
3
The reactive extraction of phenylalanine with Aliquat 336: buffer co-extraction equilibrium and mass transfer kinetics.用Aliquat 336对苯丙氨酸进行反应萃取:缓冲剂共萃取平衡及传质动力学
Biotechnol Bioeng. 2000 Sep 5;69(5):469-77.
4
Studies on the kinetics and equilibrium of the solvent extraction of chromium(III) from alkaline aqueous solutions of different composition in the system with Aliquat 336.研究了从不同组成的碱性水溶液中用 Aliquat 336 萃取铬(III)的动力学和平衡。
J Hazard Mater. 2011 Dec 30;198:257-68. doi: 10.1016/j.jhazmat.2011.10.038. Epub 2011 Oct 17.
5
Interfacial mass transfer in extraction of amino acid by ALIQUAT 336 in organic phase.用有机相中的ALIQUAT 336萃取氨基酸时的界面传质
J Chem Technol Biotechnol. 1990;48(4):415-26. doi: 10.1002/jctb.280480404.
6
Co-extraction during reactive extraction of phenylalanine using Aliquat 336: interfacial mass transfer.
Biotechnol Prog. 2003 Mar-Apr;19(2):469-76. doi: 10.1021/bp025630e.
7
Modeling of liquid-liquid hollow fiber supported membrane equilibrium including the non-ideality of the aqueous and organic phases in the recovery systems of radionuclides in sulphate-halide/aliquat-336 in O-xylene.
Appl Radiat Isot. 2024 May;207:111263. doi: 10.1016/j.apradiso.2024.111263. Epub 2024 Feb 27.
8
Solid-phase extraction of cobalt(II) from lithium chloride solutions using a poly(vinyl chloride)-based polymer inclusion membrane with Aliquat 336 as the carrier.使用以Aliquat 336为载体的聚氯乙烯基聚合物包容膜从氯化锂溶液中固相萃取钴(II)。
Anal Sci. 2011;27(6):653-7. doi: 10.2116/analsci.27.653.
9
An Ionic Supported Liquid Membrane for the Recovery of Bisphenol A from Aqueous Solution.一种用于从水溶液中回收双酚A的离子支撑液膜。
Membranes (Basel). 2022 Sep 8;12(9):869. doi: 10.3390/membranes12090869.
10
Liquid-Liquid Extraction-Chromogenic System for Vanadium(V) Based on 4-(2-thiazolylazo)orcinol (TAO) and Aliquat 336.基于4-(2-噻唑基偶氮)邻苯二酚(TAO)和Aliquat 336的钒(V)液-液萃取-显色体系
Acta Chim Slov. 2018 Dec;65(4):847-852.