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Energy-efficient heat pump-assisted pre-concentration integrated with sequential [EMIM][BF4] and ethylene glycol-based extractive distillation for enhanced recovery of ethanol and isopropyl alcohol from wastewater
被引:0
|作者:
Guo, Chao
[1
]
Zheng, Yong
[1
]
Wang, Shuai
[1
]
He, Ge
[2
]
Gui, Chengmin
[3
]
机构:
[1] Chengdu Univ Technol, Coll Mat & Chem & Chem Engn, Chengdu 610059, Peoples R China
[2] Sichuan Univ, Coll Chem Engn, Chengdu 610065, Peoples R China
[3] Anhui Univ, Sch Chem & Chem Engn, Hefei 230601, Peoples R China
基金:
中国国家自然科学基金;
关键词:
Ionic liquid;
Azeotrope;
Extractive distillation;
Double entrainers;
Pre-concentration;
Near-boiling mixture;
VAPOR-LIQUID-EQUILIBRIA;
IONIC LIQUIDS;
UNIFAC MODEL;
SEPARATION;
DEHYDRATION;
SELECTION;
D O I:
10.1016/j.seppur.2024.130073
中图分类号:
TQ [化学工业];
学科分类号:
0817 ;
摘要:
Recovering ethanol and isopropyl alcohol (IPA) from wastewater offers significant economic and environmental advantages. In this work, 1-ethyl-3-methylimidazolium tetrafluoroborate ([EMIM][BF4]) 4 ]) and ethylene glycol (EG) are proposed as double entrainers for separating IPA/ethanol/water mixtures. The novel process sequentially uses [EMIM][BF4] 4 ] to separate ethanol/water and IPA/water azeotropes, followed by EG for near-boiling mixture of ethanol/IPA. Energy-economic comparisons of extractive distillation process using single and double entrainers are performed. To address the issue of high water content in mixtures, the heat pump-assisted pre- concentration (HPP) integrated with extractive distillation processes are proposed. Subsequently, the effect of water content in the mixtures on process performances are analyzed. The results indicate that compared to using a single entrainer [EMIM][BF4] 4 ] or EG process, the double entrainers process reduces energy cost and total annual cost (TAC) by 19.9% to 45.3% and 18.6% to 52.7%, respectively. The HPP scheme effectively reduces the mole fraction of water from 60% to 26.05%, further decreasing energy costs by 4.2% to 22.2%. The energy cost and TAC of the double entrainers process decreases by 4.8% to 50%, and 2.8% to 52.1% compared with the single entrainer process under HPP schemes. The double entrainers [EMIM][BF4]-EG 4 ]-EG process shows promising prospects from energy and economic perspectives.
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页数:15
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