Microwave-Assisted Transesterification of Enriched Crude Glycerol to Glycerol Carbonate: Optimization, Simulation, and Techno-Economic Evaluation

This research presents a novel approach to create glycerol carbonate (GC) from refined crude glycerol through microwave-assisted transesterification. It integrates experimental enhancement with techno-economic and ecological assessments. The refining procedure raised the glycerol content from 40.56 wt % to 98.83 wt %, ensuring a high-quality input. Response surface methodology (RSM) was used to aid optimization of the reaction conditions. The best conditions were a 6.5 wt % catalyst concentration, 2.74:1 dimethyl carbonate:glycerol molar ratio, a reaction temperature of 78.36 °C, and a reaction duration of 36.5 min, which gave a 73.65% yield of GC. Experimental data matched the model estimates under these settings, validating the RSM dependability. The activation energy was calculated as 54.57 kJ/mol. A techno-economic assessment, performed using the Aspen Plus V11 software, revealed that the process is a viable investment possibility, with a net present value of $31.23 million, an internal rate of return of 27.96%, and a payback duration of 4.11 years. A sensitivity assessment revealed that the GC selling price considerably affected the profit and that the CO<sub>2</sub> releases tied to GC creation totaled 2.11 kg CO<sub>2</sub> per kg of GC. Catalyst reuse tests over three cycles exhibited a sound steadiness, with only a 10% efficiency reduction. These outcomes display a scalable, lasting path to GC output, accentuating industrial practicality besides economic strength.

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Publication Details

Journal
ACS Omega
Published
2025-09-20
DOI
https://doi.org/10.1021/acsomega.5c06226
Citations
2
Primary Topic
Carbon dioxide utilization in catalysis
Type
article
Field-Weighted Citation Impact
1.41
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article

Microwave-Assisted Transesterification of Enriched Crude Glycerol to Glycerol Carbonate: Optimization, Simulation, and Techno-Economic Evaluation

Jakkrapong Jitjamnong, Napaphat Kongrit, Suriati Sufian, Phonsan Saetiao et al.
2 citations
ACS Omega
Carbon dioxide utilization in catalysis
1.41
article

Microwave-Assisted Transesterification of Enriched Crude Glycerol to Glycerol Carbonate: Optimization, Simulation, and Techno-Economic Evaluation

Jakkrapong Jitjamnong, Napaphat Kongrit, Suriati Sufian, Phonsan Saetiao, Panadda Solod
article en
2 citations

Abstract

This research presents a novel approach to create glycerol carbonate (GC) from refined crude glycerol through microwave-assisted transesterification. It integrates experimental enhancement with techno-economic and ecological assessments. The refining procedure raised the glycerol content from 40.56 wt % to 98.83 wt %, ensuring a high-quality input. Response surface methodology (RSM) was used to aid optimization of the reaction conditions. The best conditions were a 6.5 wt % catalyst concentration, 2.74:1 dimethyl carbonate:glycerol molar ratio, a reaction temperature of 78.36 °C, and a reaction duration of 36.5 min, which gave a 73.65% yield of GC. Experimental data matched the model estimates under these settings, validating the RSM dependability. The activation energy was calculated as 54.57 kJ/mol. A techno-economic assessment, performed using the Aspen Plus V11 software, revealed that the process is a viable investment possibility, with a net present value of $31.23 million, an internal rate of return of 27.96%, and a payback duration of 4.11 years. A sensitivity assessment revealed that the GC selling price considerably affected the profit and that the CO<sub>2</sub> releases tied to GC creation totaled 2.11 kg CO<sub>2</sub> per kg of GC. Catalyst reuse tests over three cycles exhibited a sound steadiness, with only a 10% efficiency reduction. These outcomes display a scalable, lasting path to GC output, accentuating industrial practicality besides economic strength.

ACS OmegaVol. 10(38)
Universiti Teknologi Petronas (MY), Rajamangala University of Technology Srivijaya (TH)
Openalex Percentile: Top 20%
Carbon dioxide utilization in catalysis
1.41
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