羧化
过程(计算)
碳酸盐
过程集成
乙烯
生产(经济)
过程开发
化学
碳酸乙烯酯
可持续发展
可持续生产
工艺工程
化学工程
环境科学
废物管理
催化作用
有机化学
计算机科学
工程类
物理化学
法学
经济
电极
宏观经济学
操作系统
电解质
政治学
作者
Wei Lin Ng,Zi Xuen Er,Dhibasri Chandrakumar,Adrian Chun Minh Loy,Jitraporn Pimm Vongsvivut,Sankar Bhattacharya
标识
DOI:10.1021/acssuschemeng.4c06519
摘要
CO 2 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 CeO 2 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.
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