TY - JOUR
T1 - Sustainable Route of Ethylene Carbonate Production via CO2 Carboxylation
T2 - Process Development, Process Integration, and Economic Analysis
AU - Ng, Wei Lin
AU - Er, Zi Xuen
AU - Chandrakumar, Dhibasri
AU - Loy, Adrian Chun Minh
AU - Vongsvivut, Jitraporn
AU - Bhattacharya, Sankar
N1 - Publisher Copyright:
© 2024 American Chemical Society.
PY - 2024/12/6
Y1 - 2024/12/6
N2 - CO2 carboxylation with ethylene glycol (EG) to synthesize ethylene carbonate (EC) is an ecofriendly alternative to traditional methods that rely on toxic, fossil-based epoxides. In this study, the sustainable production of EC for large-scale feasibility and economic viability through experimental and simulation analyses were developed. Our experimental work (case A) using a CeO2 nanorod catalyst achieved the highest EC production (0.072 mmol EC/g EG) reported in the literature without a dehydrating agent. For a comprehensive evaluation, we conducted a techno-economic comparative assessment against a study with the best EC yield using 2-cyanopyridine (case B). Process integration for both cases was implemented through a heat exchanger network system (HENS) design, achieving ∼60% in heat recovery, and further exergy analysis reported an efficiency of >90%. Although case B achieved near-perfect conversion efficiency with 2-cyanopyridine, its economic viability was less promising than case A. With current technology, neither case is feasible for commercialization at an annual EC production of 5 ktonne. The minimum selling price of EC must exceed AUD 10.20/kg for case A and AUD 26.50/kg for case B. Our results suggest that eliminating hazardous 2-cyanopyridine is possible, with further recommendations to fully realize the profitability of this production’s approach.
AB - CO2 carboxylation with ethylene glycol (EG) to synthesize ethylene carbonate (EC) is an ecofriendly alternative to traditional methods that rely on toxic, fossil-based epoxides. In this study, the sustainable production of EC for large-scale feasibility and economic viability through experimental and simulation analyses were developed. Our experimental work (case A) using a CeO2 nanorod catalyst achieved the highest EC production (0.072 mmol EC/g EG) reported in the literature without a dehydrating agent. For a comprehensive evaluation, we conducted a techno-economic comparative assessment against a study with the best EC yield using 2-cyanopyridine (case B). Process integration for both cases was implemented through a heat exchanger network system (HENS) design, achieving ∼60% in heat recovery, and further exergy analysis reported an efficiency of >90%. Although case B achieved near-perfect conversion efficiency with 2-cyanopyridine, its economic viability was less promising than case A. With current technology, neither case is feasible for commercialization at an annual EC production of 5 ktonne. The minimum selling price of EC must exceed AUD 10.20/kg for case A and AUD 26.50/kg for case B. Our results suggest that eliminating hazardous 2-cyanopyridine is possible, with further recommendations to fully realize the profitability of this production’s approach.
KW - CO carboxylation
KW - exergy analysis
KW - green chemistry
KW - heat integration
KW - techno-economic analysis
UR - http://www.scopus.com/inward/record.url?scp=85211452249&partnerID=8YFLogxK
U2 - 10.1021/acssuschemeng.4c06519
DO - 10.1021/acssuschemeng.4c06519
M3 - Article
AN - SCOPUS:85211452249
SN - 2168-0485
VL - 12
SP - 18320
EP - 18334
JO - ACS Sustainable Chemistry and Engineering
JF - ACS Sustainable Chemistry and Engineering
IS - 51
ER -