• 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

基于对映点的差分进化算法在生物柴油生产相关化合物气液平衡建模中的参数估计

Parameter estimation in vapor-liquid equilibrium modeling of compounds related to biodiesel production using opposite point-based differential evolution algorithm.

作者信息

Yadav Swati, Angira Rakesh

机构信息

Process Systems Engineering Laboratory, University School of Chemical Technology, Guru Gobind Singh Indraprastha University, Sector 16-C, Dwarka, Delhi, 110078, India.

出版信息

Environ Sci Pollut Res Int. 2024 Oct 29. doi: 10.1007/s11356-024-35257-8.

DOI:10.1007/s11356-024-35257-8
PMID:39470911
Abstract

Biodiesel stands out as the most favorable alternatives to fossil-derived diesel, offering a multitude of environmental benefits. At various stages of biodiesel production, the separation processes necessitate thermodynamic models with the capability to correlate and predict phase equilibria of mixtures. In this study, application of the classical differential evolution (DE) and its new enhanced version, the OPDE algorithm, for modeling vapor-liquid equilibrium (VLE) associated with components related to biodiesel production is presented. The algorithms were analysed and contrasted in terms of their performance, in estimating parameters for Wilson, NRTL and UNIFAC models. Additionally, classical least-squares (LS) and error-in-variable (EIV) approaches were examined and compared. Also, VLE datasets for a specific system have been merged, and parameters have been estimated. The findings suggest that parameters obtained through LS approach align with those reported in literature, indicating faster convergence in all problems. In contrast, the EIV approach achieved a higher objective function value compared to the LS approach, exhibiting low deviation. OPDE outperformed DE in terms of performance. The enhancement in RMSTD value has been found within range 91%-99% for EIV approach. Further, novel findings derived from some of the studied VLE datasets are presented.

摘要

生物柴油是化石衍生柴油最有利的替代品之一,具有诸多环境效益。在生物柴油生产的各个阶段,分离过程需要能够关联和预测混合物相平衡的热力学模型。本研究介绍了经典差分进化(DE)及其新的增强版本OPDE算法在与生物柴油生产相关组分的气液平衡(VLE)建模中的应用。对这些算法在估计Wilson、NRTL和UNIFAC模型参数方面的性能进行了分析和对比。此外,还研究并比较了经典最小二乘法(LS)和变量误差(EIV)方法。同时,合并了特定系统的VLE数据集并估计了参数。结果表明,通过LS方法获得的参数与文献报道的参数一致,表明在所有问题中收敛速度更快。相比之下,EIV方法与LS方法相比目标函数值更高,偏差较小。OPDE在性能方面优于DE。对于EIV方法,RMSTD值的提高幅度在91%-99%范围内。此外,还展示了一些研究的VLE数据集得出的新发现。

相似文献

1
Parameter estimation in vapor-liquid equilibrium modeling of compounds related to biodiesel production using opposite point-based differential evolution algorithm.基于对映点的差分进化算法在生物柴油生产相关化合物气液平衡建模中的参数估计
Environ Sci Pollut Res Int. 2024 Oct 29. doi: 10.1007/s11356-024-35257-8.
2
Using the group contribution method to predict the flash temperature of biodiesel and ethanol mixtures.使用基团贡献法预测生物柴油和乙醇混合物的闪蒸温度。
Heliyon. 2024 Aug 16;10(17):e36453. doi: 10.1016/j.heliyon.2024.e36453. eCollection 2024 Sep 15.
3
Isobaric vapor-liquid equilibrium for methyldichlorosilane-dimethyldichlorosilane-benzene system.甲基二氯硅烷-二甲基二氯硅烷-苯体系的等压气液平衡
J Zhejiang Univ Sci B. 2005 Oct;6(10):1033-7. doi: 10.1631/jzus.2005.B1033.
4
Separation of the Azeotropic Mixture Methanol and Toluene Using Extractive Distillation: Entrainer Determination, Vapor-Liquid Equilibrium Measurement, and Modeling.采用萃取精馏分离甲醇和甲苯共沸混合物:夹带剂的确定、气液平衡测量及建模
ACS Omega. 2021 Dec 9;6(50):34736-34743. doi: 10.1021/acsomega.1c05164. eCollection 2021 Dec 21.
5
The Effects of NaI, KBr, and KI Salts on the Vapor-Liquid Equilibrium of the HO+CHOH System.碘化钠、溴化钾和碘化钾盐对HO+CHOH体系气液平衡的影响。
Front Chem. 2020 Apr 7;8:192. doi: 10.3389/fchem.2020.00192. eCollection 2020.
6
Multiphase Behavior of the Water + 1-Butanol + Deep Eutectic Solvent Systems at 101.3 kPa.101.3 kPa下,水 + 正丁醇 + 低共熔溶剂体系的多相行为
Molecules. 2024 Oct 11;29(20):4814. doi: 10.3390/molecules29204814.
7
LLE experimental data, thermodynamic modeling and sensitivity analysis in the ethyl biodiesel from macauba pulp oil settling step.液化酯交换(LLE)实验数据、热力学建模和在油麻藤果肉油沉降步骤中制取乙酯生物柴油的敏感性分析。
Bioresour Technol. 2013 Mar;131:468-75. doi: 10.1016/j.biortech.2012.12.190. Epub 2013 Jan 11.
8
Modeling Binary and Multicomponent Systems Containing Supercritical CO with Polyethylene Glycols and Compounds Relevant to the Biodiesel Production.建模含超临界 CO2 的二元和多组分体系与聚乙二醇及与生物柴油生产相关的化合物。
Molecules. 2022 Sep 7;27(18):5785. doi: 10.3390/molecules27185785.
9
Development of Anhydrous Ethanol Purification: Reduction of Acetal Content and Vapor-Liquid Equilibrium Study of the Ethanol-Acetal Binary System.无水乙醇纯化的发展:缩醛含量的降低及乙醇-缩醛二元体系的气液平衡研究
ACS Omega. 2021 Jan 5;6(2):1289-1298. doi: 10.1021/acsomega.0c04750. eCollection 2021 Jan 19.
10
Liquid-Liquid Equilibrium of Sesame Fatty Acid (Ethyl and Methyl) Ester + Glycerol + Ethanol/Methanol Mixtures at Different Temperatures.不同温度下芝麻脂肪酸(乙酯和甲酯)+甘油+乙醇/甲醇混合物的液-液平衡
Molecules. 2024 Jul 3;29(13):3167. doi: 10.3390/molecules29133167.