Issue 25, 2024

Optimization of the catalytic production of methyl stearate by applying response surface Box–Behnken design: an intensified green option for high-cetane biofuel manufacture

Abstract

To enhance the efficiency of processes by decreasing the reaction severity and energy consumption, and reducing the equipment size, facilities' space and operation cost, process intensification is an increasingly used option in the chemical industry. Within this framework and in agreement with some of the green chemistry principles (design for energy efficiency and use of renewable feedstocks), this work deals with the implementation of high-shear mixing (HSM) to intensify the homogeneous esterification of stearic acid (SA) with methanol to methyl stearate, a high-cetane number alkyl ester suitable to be added into biofuel streams. The response surface Box–Behnken design (BBD) is applied to quantify the main effects and two-way interactions of four key input reaction factors: methanol : SA ratio (7–16 mol mol−1), catalyst mass (0.25–4.0 wt%), temperature (40–60 °C), time (1–12 min), and to approximate the optimal conditions on the intensified SA esterification. The statistical BBD results indicates that the four linear effects, two of the four possible quadratic effects (catalyst mass and temperature) and only one (catalyst mass–time) of the six existing two-way interactions are statistically relevant at the 95% confidence level. Catalyst mass is the most influencing factor in the reaction, followed by methanol : SA ratio, temperature, and time. The proposed second-order regression model predicts that the intensified esterification requires only 12 min to practically convert all SA (99% ± 6.8%) running the reaction at 12.4 methanol : SA ratio, 4 wt% catalyst mass, 60 °C and 500 rpm, a value experimentally validated (93.2% ± 0.7%). Under these conditions and with the assistance of HSM, the typical reaction length of conventional heterogeneous and homogeneous-phase esterification processes decreases from 5 to 117 and 35 to 90 times, respectively.

Graphical abstract: Optimization of the catalytic production of methyl stearate by applying response surface Box–Behnken design: an intensified green option for high-cetane biofuel manufacture

Supplementary files

Article information

Article type
Paper
Submitted
13 Apr 2024
Accepted
21 May 2024
First published
05 Jun 2024
This article is Open Access
Creative Commons BY-NC license

RSC Adv., 2024,14, 17990-18002

Optimization of the catalytic production of methyl stearate by applying response surface Box–Behnken design: an intensified green option for high-cetane biofuel manufacture

F. M. Reyes-Cruz, J. D. Santamaría-Juárez, M. Sánchez-Cantú and R. Quintana-Solórzano, RSC Adv., 2024, 14, 17990 DOI: 10.1039/D4RA02750G

This article is licensed under a Creative Commons Attribution-NonCommercial 3.0 Unported Licence. You can use material from this article in other publications, without requesting further permission from the RSC, provided that the correct acknowledgement is given and it is not used for commercial purposes.

To request permission to reproduce material from this article in a commercial publication, please go to the Copyright Clearance Center request page.

If you are an author contributing to an RSC publication, you do not need to request permission provided correct acknowledgement is given.

If you are the author of this article, you do not need to request permission to reproduce figures and diagrams provided correct acknowledgement is given. If you want to reproduce the whole article in a third-party commercial publication (excluding your thesis/dissertation for which permission is not required) please go to the Copyright Clearance Center request page.

Read more about how to correctly acknowledge RSC content.

Social activity

Spotlight

Advertisements