热集成及热泵强化低共熔溶剂萃取精馏分离异丙醇-水Heat integration and heat pump intensified extractive distillation for isopropanol-water separation using deep eutectic solvents as entrainer
王菊,许洁,杜春华,吴现力
摘要(Abstract):
低共熔溶剂(DESs)作为一种新型环境友好溶剂,在萃取精馏中展现出巨大潜力。通过Aspen Plus流程模拟软件设计并优化了以DESs(氯化胆碱/三甘醇,物质的量比为1∶3)为萃取剂的异丙醇-水萃取精馏分离工艺。以年度总费用(TAC)最小为目标,采用序贯迭代法对进料位置、萃取剂用量、萃取剂温度、理论板数和回流比进行优化。模拟结果表明,与以传统溶剂乙二醇(EG)为萃取剂的工艺相比,该工艺所需的塔板数、回流比显著减小,TAC可降低20.95%。为进一步挖掘节能潜力,构建了结合热集成与热泵的两种强化工艺。全面的对比分析表明,热集成-热泵辅助萃取精馏工艺较以EG为萃取剂的传统工艺的能耗、TAC及有效能损失分别降低了46.35%、31.10%和39.33%。DESs在经济性与环境友好性方面展现出替代传统萃取剂的潜力。
关键词(KeyWords): 低共熔溶剂;萃取精馏;异丙醇-水;热集成;热泵
基金项目(Foundation): 国家自然科学基金(21706142);; 山东省自然科学基金(ZR2025MS250);; 青岛农业大学高层次人才科研基金(6631114316,6631116020)
作者(Author): 王菊,许洁,杜春华,吴现力
参考文献(References):
- [1]郭义敏,邹昀,张秀钰,等.乙酸+异丙醇酯化体系中汽液平衡测定及萃取精馏[J].高校化学工程学报,2024,38(2):172-183.GUO Y M, ZOU Y, ZHANG X Y, et al. Determination of vapor-liquid equilibrium of the acetic acid+isopropanol esterification system and extractive distillation[J]. Journal of Chemical Engineering of Chinese Universities,2024,38(2):172-183.
- [2]LI Y, YE Q, WANG N, et al. Energy-efficient extractive distillation combined with heat-integrated and intermediate reboilers for separating acetonitrile/isopropanol/water mixture[J]. Separation and Purification Technology,2021,262:118343-118356.
- [3]QI J,LI Y,XUE J,et al. Comparison of heterogeneous azeotropic distillation and energy-saving extractive distillation for separating the acetonitrile-water mixtures[J]. Separation and Purification technology,2020,238:116487-116498.
- [4]孔洁,李沅欣,孙兰义.萃取精馏分离丙酮-正庚烷的模拟与控制[J].化工进展,2025,44(3):1253-1262.KONG J, LI Y X, SUN L Y. Simulation and control of acetone/n-heptane separation by extractive distillation[J]. Chemical Industry and Engineering Progress,2025,44(3):1253-1262.
- [5]AYUSO M, CA??ADA-BARCALA A, LARRIBA M, et al. Enhanced separation of benzene and cyclohexane by homogeneous extractive distillation using ionic liquids as entrainers[J]. Separation and Purification Technology,2020,240:116583.
- [6]QI J, ZHU R, HAN X, et al. Ionic liquid extractive distillation for the recovery of diisopropyl ether and isopropanol from industrial effluent:Experiment and simulation[J]. Journal of Cleaner Production,2020,254:120132.
- [7]李鑫,王维,张羽,等.分离乙酸乙酯+乙醇+水体系:离子液体筛选、汽液相平衡和过程模拟[J].化工进展,2025,44(1):75-85.LI X, WANG W, ZHANG Y, et al. Separation of ethyl acetate+ethanol+water system:Ionic liquids screening, vapor liquid equilibrium and process simulation[J]. Chemical Industry and Engineering Progress,2025,44(1):75-85.
- [8]ORTEGA V M R,BALDIN E K,PEREIRA D P,et al. Toxicity of oleate-based amino protic ionic liquids towards Escherichia coli,Danio rerio embryos and human skin cells[J]. Journal of Hazardous Materials,2022,422:126896.
- [9]MAXIMILIAN N T W S L. Deep eutectic solvents as entrainers in extractive distiillation-A review[J]. Chemical Engineering Research and Design,2022,184:402-418.
- [10]PEI Z,CUI X L. Molecular mechanism,thermoeconomic,and environmental impact for separation of isopropanol and water using the choline-based DESs as extractants[J]. Industrial&Engineering Chemistry Research,2020,59:16077-16087.
- [11]ABBAS Q, BINDER L. Synthesis and characterization of choline chloride based binary mixtures[J]. ECS Transactions, 2010,33(7):49-59.
- [12]AISSAOUI T, BENGUERBA Y, ALNASHEF I M. Theoretical investigation on the microstructure of triethylene glycol based deep eutectic solvents:COSMO-RS and TURBOMOLE prediction[J]. Journal of Molecular Structure,2017,1141:451-456.
- [13]ALKHATIB I I I, BAHAMON D, LLOVELL F, et al. Perspectives and guidelines on thermodynamic modelling of deep eutectic solvents[J]. Journal of Molecular Liquids,2020,298:112183-112200.
- [14]LERON R B, LI M. Molar heat capacities of choline chloride-based deepeutectic solvents and their binary mixtures with water[J].Thermochimica Acta,2012,530:52-57.
- [15]MIRZA N R,NICHOLAS N J,WU Y,et al. Estimation of normal boiling temperatures,critical properties,and acentric factors of deep eutectic solvents[J]. Journal of Chemical&Engineering Data,2015,60:1844-1854.
- [16]NASER J, MIALLI F S, GANO Z S. Molar heat capacity of selected type III deep eutectic solvents[J]. Journal of Chemical&Engineering Data,2016,61:1608-1615.
- [17]RODRIGUEZ N R,GONZ??LEZ A S B,TIJSSEN P M A,et al. Low transition temperature mixtures(LTTMs)as novel entrainers in extractive distillation[J]. Fluid Phase Equilibria,2015,385:72-78.
- [18]SHAHBAZ K, MJALLI F S, VAKILI N G, et al. Thermogravimetric measurement of deep eutectic solvents vapor pressure[J].Journal of Molecular Liquids,2016,222:61-66.
- [19]WU S,CAPARANGA A R,LERON R B,et al. Vapor pressure of aqueous choline chloride-based deep eutectic solvents(ethaline,glyceline,maline and reline)at 30-70℃[J]. Thermochimica Acta,2012,544:1-5.
- [20]XIN K, ROGHAIR I, GALLUCCI F, et al. Total vapor pressure of hydrophobic deep eutectic solvents:Experiments and modelling[J]. Journal of Molecular Liquids,2021,325:115227-115235.
- [21]ZHU C,XUE S,IKRAM R,et al. Experimental study on isobaric molar heat capacities of a deep eutectic solvent:Choline chloride+ethylene glycol[J]. Journal of Chemical&Engineering Data,2020,65:690-695.
- [22]MA S T, HOU Y F, SUN Y H, et al. Simulation and experiment for ethanol dehydration using low transition temperature mixtures(LTTMs)as entrainers[J]. Chemical Engineering&Processing:Process Intensification,2017,121:71-80.
- [23]FONTANA M,MARCHESAN A N,FILHO R M,et al. Extractive distillation to produce anhydrous bioethanol with choline chloride with urea(1∶2)as a solvent:a comparative evaluation of the equilibrium and the rate-based models[J]. Chemical Engineering and Processing-Process Intensification,2021,168:108580-108595.
- [24]HAN D M, CHEN Y H. Combining the preconcentration column and recovery column for the extractive distillation of ethanol dehydration with low transition temperature mixtures as entrainers[J]. Chemical Engineering&Processing:Process Intensification,2018,131:203-214.
- [25]李源.异丙醇-水体系和正己烷-乙醇体系LTTMs溶剂筛选研究[D].青岛:中国石油大学(华东),2018.LI Y. Solvent screening of isopropanol-water system and hexane-ethanol system using lttms as separation agents[D]. Qingdao:China University of Petroleum(East China),2018.
- [26]JIANG H,XU D,ZHANG L,et al. Vapor-liquid phase equilibrium for separation of isopropanol from its aqueous solution by choline chloride-based deep eutectic solvent selected by COSMO-SAC model[J]. Journal of Chemical&Engineering Data,2019,64:1338-1348.
- [27]LUYBEN W L. Comparison of extractive distillation and pressure-swing distillation for acetone/chloroform separation[J]. Computers&Chemical Engineering,2013,50:1-7.
- [28]XU H,WANG X,ZOU Y,et al. Exergy,economic and environmental assessment of sec-butyl acetate hydrolysis to sec-butyl alcohol using a combined reaction and extractive distillation system[J]. Fuel,2021,286-297.
- [29]HASHEMI M, POURFAYAZ F, MEHRPOOYA M. Energy, exergy, exergoeconomic and sensitivity analyses of modified Claus process in a gas refinery sulfur recovery unit[J]. Journal of Cleaner Production,2019,220:1071-1087.
- [30]LI X, YE Q, LI J, et al. Investigation of energy-efficient heat pump assisted heterogeneous azeotropic distillation for separating of acetonitrile/ethyl acetate/n-hexane mixture[J]. Chinese Journal of Chemical Engineering, 2023, 55:20-33.
- [31]ZHAI J,CHEN X,SUN X,et al. Economically and thermodynamically efficient pressure-swing distillation with heat integration and heat pump techniques[J]. Applied Thermal Engineering, 2023, 218:119389.
- [32]ZHANG Q, YANG S, HI P, et al. Economically and thermodynamically efficient heat pump-assisted side-stream pressure-swing istillation arrangement for separating a maximum-boiling azeotrope[J]. Applied Thermal Engineering, 2020, 173:115228.
- [33]PLE??U V,BONET RUIZ A E,BONET J,et al. Simple equation for suitability of heat pump use in distillation[J]. Computer Aided hemical Engineering, 2014, 33:1327-1332.