首页 | 本学科首页   官方微博 | 高级检索  
     

基于代理模型的含盐废水多级纳滤系统的过程优化设计
引用本文:陆至彬,谢星,鲁思达,何畅,张冰剑,陈清林.基于代理模型的含盐废水多级纳滤系统的过程优化设计[J].化工学报,2021,72(3):1400-1408.
作者姓名:陆至彬  谢星  鲁思达  何畅  张冰剑  陈清林
作者单位:1.中山大学材料科学与工程学院,广东 广州 510275;2.西安航天源动力工程有限公司,陕西 西安 710000;3.中山大学 化学工程与技术学院,广东 珠海 519082;4.广东省石化过程节能工程技术研究中心,广东 广州 510275
基金项目:国家自然科学基金项目(51776228);中央高校基本科研业务费专项资金(20lgpy01)
摘    要:基于道南细孔-介电DSPM-DE模型,开展了工业含盐废水多级纳滤分离系统的代理模型构建与优化研究。首先,利用高维模型表征的数学建模方法,构建与原有纳滤理论模型有高拟合度的高精度代理模型。基于此代理模型,进一步构建膜法分盐工艺中的多级纳滤分离的数学优化模型,并以分离单位质量NaCl的比能耗为优化目标,讨论在给定设计参数的条件下进料液中Cl-]/SO42-]的变化对不同级数纳滤系统的分盐性能及最优操作条件的影响。优化结果显示,进料Cl-]/SO42-]的增加有利于提高NaCl总回收率和降低分盐比能耗。在相同的纳滤膜投资成本下,双级系统在降低能耗方面更胜一筹,与单级系统相比最高可节能5.84%。

关 键 词:废水  纳滤  分盐  代理模型  比能耗  优化  节能  
收稿时间:2020-06-08

Surrogate model-based optimal design of multi-stage nanofiltration separation system for saline wastewater
LU Zhibin,XIE Xing,LU Sida,HE Chang,ZHANG Bingjian,CHEN Qinglin.Surrogate model-based optimal design of multi-stage nanofiltration separation system for saline wastewater[J].Journal of Chemical Industry and Engineering(China),2021,72(3):1400-1408.
Authors:LU Zhibin  XIE Xing  LU Sida  HE Chang  ZHANG Bingjian  CHEN Qinglin
Affiliation:1.School of Materials Science and Engineering, Sun Yat-sen University, Guangzhou 510275, Guangdong, China;2.Xi’an Aerospace Yuan Dongli Engineering Co. , Ltd. , Xi’an 710000, Shanxi, China;3.School of Chemical Engineering and Technology, Sun Yat-sen University, Zhuhai 519082, Guangdong, China;4.Guangdong Engineering Center for Petrochemical Energy Conservation, Guangzhou 510275, Guangdong, China
Abstract:Based on Donnan steric pore model with dielectric exclusion (DSPM-DE), this work develops a surrogate model for the multi-stage nanofiltration separation of industrial saline wastewater. Firstly, a high-fidelity surrogate model with a high fitting degree is established to describe the DSPM-DE-based nanofiltration process via high dimensional model representation. On this basis, we construct the optimization model of multi-stage nanofiltration separation for minimizing the specific energy consumption (SEC) of unit NaCl separated. The impacts of the changing feed ratio Cl-]/SO42-] on the separation performance and optimal operating conditions of the nanofiltration system are investigated under the given design parameters. The results indicate that an increased feed ratio Cl-]/SO42-] is beneficial to improve the total recovery of NaCl and to reduce the SEC. Under the same investment cost of nanofiltration membranes, the two-stage system is superior in reducing energy consumption, and can save up to 5.84% compared with the single-stage system.
Keywords:wastewater  nanofiltration  salts separation  surrogate model  specific energy consumption  optimization  energy saving  
点击此处可从《化工学报》浏览原始摘要信息
点击此处可从《化工学报》下载全文
设为首页 | 免责声明 | 关于勤云 | 加入收藏

Copyright©北京勤云科技发展有限公司  京ICP备09084417号