Abstract
Many studies have investigated the conversion of biomass derivatives to value-added products. However, the influence of different factors on the reaction outcomes of these often-complex systems is not well understood. Herein, a statistical design of experiments—specifically, response surface methodology—is applied to the glycerol electrooxidation reaction in a flow electrolyzer. Four operational variables (glycerol concentration, NaOH concentration, flow rate, and catalyst loading) were investigated for their effects on measurable responses of the electrochemical reaction: current density and Faradaic efficiency to a given product. Independent optimizations of current density and Faradaic efficiency, as well as simultaneous optimization of both, were investigated. Each optimization was evaluated using response surface coefficients to analyze sensitivity and simulated runs to visualize the parameter space. These evaluations revealed contradictions in operating conditions required to simultaneously maximize current density and Faradaic efficiency to C3 products glycerate and lactate, leading to low current densities and Faradaic efficiencies. However, simultaneously maximizing current density and Faradaic efficiency to C1 product formate led to high current densities and Faradaic efficiencies. These insights guide tuning GEOR production to maximize overall reactor performance. Furthermore, this study outlines a framework for experimental evaluation and optimization of other electrolysis chemistries.
| Original language | English |
|---|---|
| Article number | 063506 |
| Journal | Journal of the Electrochemical Society |
| Volume | 171 |
| Issue number | 6 |
| DOIs | |
| State | Published - Jun 3 2024 |
Funding
The authors acknowledge funding from the National Science Foundation through the EFRI-DCheM program, grant #2029326 (Renewable-Energy Driven Electrocatalytic Co-Conversion of CO2 and Regional Feedstocks to Chemicals and Fuels) and a TechnipFMC fellowship to RNG. We also acknowledge the use of facilities and instrumentation supported by NSF through the University of Illinois Materials Research Science and Engineering Center DMR-2309037. The basis code for the MATLAB scripts used for HPLC chromatogram analysis were generously provided by Tom O’Haver, University of Maryland-College Park. We also appreciate helpful feedback and many fruitful conversations with Raghuram Gaddam, Adam Sibal, Joaquín Rodríguez-López, and Ashlynn Stillwell. The authors acknowledge funding from the National Science Foundation through the EFRI-DCheM program, grant #2029326 (Renewable-Energy Driven Electrocatalytic Co-Conversion of CO and Regional Feedstocks to Chemicals and Fuels) and a TechnipFMC fellowship to RNG. We also acknowledge the use of facilities and instrumentation supported by NSF through the University of Illinois Materials Research Science and Engineering Center DMR-2309037. The basis code for the MATLAB scripts used for HPLC chromatogram analysis were generously provided by Tom O’Haver, University of Maryland-College Park. We also appreciate helpful feedback and many fruitful conversations with Raghuram Gaddam, Adam Sibal, Joaquín Rodríguez-López, and Ashlynn Stillwell. 2
Keywords
- electrifying chemical manufacturing
- electrocatalysis
- electrochemical engineering
- glycerol oxidation
- response surface methodology
- statistical design of experiments
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