Dissecting steric and polar substituent effects in linear free energy Relationships: Re-Assessment of the Taft equation with Temperature-Dependent kinetic modeling
Sindi Baco , Mélanie Mignot , Christoph Held , Julien Legros , Sébastien Leveneur
{"title":"Dissecting steric and polar substituent effects in linear free energy Relationships: Re-Assessment of the Taft equation with Temperature-Dependent kinetic modeling","authors":"Sindi Baco , Mélanie Mignot , Christoph Held , Julien Legros , Sébastien Leveneur","doi":"10.1016/j.ces.2025.122700","DOIUrl":null,"url":null,"abstract":"<div><div>Kinetic models are vital for developing process flow diagrams that support cost, risk, and environmental assessments, but constructing them is time-consuming, particularly when screening multiple substituents or solvents. Linear Free Energy Relationships (LFERs) can reduce experimental effort, yet most existing formulations neglect temperature effects. In this work, we quantify the temperature dependence (20–50 °C) of Taft’s polar (σ*) and steric (Es) substituent parameters for methyl, ethyl, n-propyl, and 2-chloroethyl groups using kinetic data from esterification and saponification of levulinate derivatives in aqueous media. Both σ* and Es varied linearly with temperature, with the strongest sensitivity observed for 2-chloroethyl (–0.007 °C<sup>−1</sup> for σ*, 0.008 °C<sup>−1</sup> for Es). Incorporating these temperature coefficients into LFER-based kinetic models enhances their predictive accuracy for reaction rates, enabling more efficient process design in biomass valorization and related chemical systems.</div></div>","PeriodicalId":271,"journal":{"name":"Chemical Engineering Science","volume":"320 ","pages":"Article 122700"},"PeriodicalIF":4.3000,"publicationDate":"2025-09-26","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":"0","resultStr":null,"platform":"Semanticscholar","paperid":null,"PeriodicalName":"Chemical Engineering Science","FirstCategoryId":"5","ListUrlMain":"https://www.sciencedirect.com/science/article/pii/S0009250925015210","RegionNum":2,"RegionCategory":"工程技术","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":null,"EPubDate":"","PubModel":"","JCR":"Q2","JCRName":"ENGINEERING, CHEMICAL","Score":null,"Total":0}
引用次数: 0
Abstract
Kinetic models are vital for developing process flow diagrams that support cost, risk, and environmental assessments, but constructing them is time-consuming, particularly when screening multiple substituents or solvents. Linear Free Energy Relationships (LFERs) can reduce experimental effort, yet most existing formulations neglect temperature effects. In this work, we quantify the temperature dependence (20–50 °C) of Taft’s polar (σ*) and steric (Es) substituent parameters for methyl, ethyl, n-propyl, and 2-chloroethyl groups using kinetic data from esterification and saponification of levulinate derivatives in aqueous media. Both σ* and Es varied linearly with temperature, with the strongest sensitivity observed for 2-chloroethyl (–0.007 °C−1 for σ*, 0.008 °C−1 for Es). Incorporating these temperature coefficients into LFER-based kinetic models enhances their predictive accuracy for reaction rates, enabling more efficient process design in biomass valorization and related chemical systems.
期刊介绍:
Chemical engineering enables the transformation of natural resources and energy into useful products for society. It draws on and applies natural sciences, mathematics and economics, and has developed fundamental engineering science that underpins the discipline.
Chemical Engineering Science (CES) has been publishing papers on the fundamentals of chemical engineering since 1951. CES is the platform where the most significant advances in the discipline have ever since been published. Chemical Engineering Science has accompanied and sustained chemical engineering through its development into the vibrant and broad scientific discipline it is today.