Concentration of 1,3-dimethyl-2-imidazolidinone in Aqueous Solutions by Sweeping Gas Membrane Distillation: From Bench to Industrial Scale

被引:8
作者
Abejon, Ricardo [1 ,2 ]
Saidani, Hafedh [1 ]
Deratani, Andre [1 ]
Richard, Christophe [3 ]
Sanchez-Marcano, Jose [1 ]
机构
[1] Univ Montpellier, Inst Europeen Membranes, CNRS, ENSCM,UMR 5635, CC 047,Pl Eugene Bataillon, F-34095 Montpellier, France
[2] Univ Cantabria, Dept Chem & Biomol Engn, Avda Los Castros S-N, E-39005 Santander, Cantabria, Spain
[3] Kermel, 20 Rue Ampere, F-68027 Colmar, France
关键词
sweeping gas membrane distillation; 1; 3-dimethyl-2-imidazolidinone; solvent dehydration; hollow-fiber membrane; multi-objective optimization; MULTIOBJECTIVE OPTIMIZATION; SEPARATION; RECOVERY; GLYCEROL; GLYCOL;
D O I
10.3390/membranes9120158
中图分类号
Q5 [生物化学]; Q7 [分子生物学];
学科分类号
071010 ; 081704 ;
摘要
Sweeping gas membrane distillation (SGMD) is a useful option for dehydration of aqueous solvent solutions. This study investigated the technical viability and competitiveness of the use of SGMD to concentrate aqueous solutions of 1,3-dimethyl-2-imidazolidinone (DMI), a dipolar aprotic solvent. The concentration from 30% to 50% of aqueous DMI solutions was attained in a bench installation with Liqui-Cel SuperPhobic (R) hollow-fiber membranes. The selected membranes resulted in low vapor flux (below 0.15 kg/h.m(2)) but were also effective for minimization of DMI losses through the membranes, since these losses were maintained below 1% of the evaporated water flux. This fact implied that more than 99.2% of the DMI fed to the system was recovered in the produced concentrated solution. The influence of temperature and flowrate of the feed and sweep gas streams was analyzed to develop simple empirical models that represented the vapor permeation and DMI losses through the hollow-fiber membranes. The proposed models were successfully applied to the scaling-up of the process with a preliminary multi-objective optimization of the process based on the simultaneous minimization of the total membrane area, the heat requirement and the air consumption. Maximal feed temperature and air flowrate (and the corresponding high operation costs) were optimal conditions, but the excessive membrane area required implied an uncompetitive alternative for direct industrial application.
引用
收藏
页数:16
相关论文
共 37 条
[1]   Design, economic evaluation and optimization of enzymatic membrane reactors for antibiotics degradation in wastewaters [J].
Abejon, R. ;
Belleville, M. P. ;
Sanchez-Marcano, J. .
SEPARATION AND PURIFICATION TECHNOLOGY, 2015, 156 :183-199
[2]  
Abejón R, 2012, COMPUT-AIDED CHEM EN, V30, P542
[3]   Recovery of volatile fruit juice aroma compounds by membrane technology: Sweeping gas versus vacuum membrane distillation [J].
Bagger-Jorgensen, Rico ;
Meyer, Anne S. ;
Pinelo, Manuel ;
Varming, Camilla ;
Jonsson, Gunnar .
INNOVATIVE FOOD SCIENCE & EMERGING TECHNOLOGIES, 2011, 12 (03) :388-397
[4]   Numerical simulation and experimental studies on heat and mass transfer using sweeping gas membrane distillation [J].
Charfi, K. ;
Khayet, M. ;
Safi, M. J. .
DESALINATION, 2010, 259 (1-3) :84-96
[5]   Dehydration of diethylene glycol using a vacuum membrane distillation process [J].
Chen, Tai-Hsiang ;
Huang, Yao-Hui .
JOURNAL OF THE TAIWAN INSTITUTE OF CHEMICAL ENGINEERS, 2017, 74 :233-237
[6]   Sweeping gas membrane distillation of sucrose aqueous solutions: Response surface modeling and optimization [J].
Cojocaru, C. ;
Khayet, M. .
SEPARATION AND PURIFICATION TECHNOLOGY, 2011, 81 (01) :12-24
[7]   OPERATING CONDITIONS INFLUENCE ON VMD AND SGMD FOR ETHANOL RECOVERY FROM AQUEOUS SOLUTIONS [J].
Cotamo-De la Espriella, Ricardo-Javier ;
Baron-Nunez, Fredy-Wsvaldo ;
Muvdi-Nova, Carlos-Jesus .
CT&F-CIENCIA TECNOLOGIA Y FUTURO, 2015, 6 (02) :69-80
[8]   Membrane distillation and related operations - A review [J].
Curcio, E ;
Drioli, E .
SEPARATION AND PURIFICATION REVIEWS, 2005, 34 (01) :35-86
[9]  
Dershmukh S.K., 2013, Journal of Chemical and Pharmaceutical Sciences, V6, P66
[10]   A framework for better understanding membrane distillation separation process [J].
El-Bourawi, M. S. ;
Ding, Z. ;
Ma, R. ;
Khayet, M. .
JOURNAL OF MEMBRANE SCIENCE, 2006, 285 (1-2) :4-29