Freestanding self-assembled sulfonated pentablock terpolymer membranes for high flux pervaporation desalination

被引:32
作者
Thomas, Elisabeth R. [1 ,6 ]
Jain, Amit [2 ,6 ]
Mann, Stewart C. [1 ,6 ]
Yang, Yi [1 ,6 ]
Green, Matthew D. [1 ,6 ]
Walker, W. Shane [5 ,6 ]
Perreault, Francois [4 ,6 ]
Lind, Mary Laura [1 ,6 ]
Verduzco, Rafael [2 ,3 ,6 ]
机构
[1] Arizona State Univ, Sch Engn Matter Transport & Energy, Tempe, AZ 85287 USA
[2] Rice Univ, Dept Chem & Biomol Engn, MS 362,6100 Main St, Houston, TX USA
[3] Rice Univ, Mat Sci & Nanoengn, MS 325,6100 Main St, Houston, TX USA
[4] Arizona State Univ, Sch Sustainable Engn & Built Environm, Tempe, AZ 85287 USA
[5] Univ Texas El Paso, Civil Engn, 500 W Univ Ave, El Paso, TX 79912 USA
[6] Rice Univ, NSF Nanosyst Engn Res Ctr Nanotechnol Enabled Wat, MS 6398,6100 Main St, Houston, TX USA
基金
美国国家科学基金会;
关键词
Pervaporation; Desalination; Self-assembled sulfonated pentablock; terpolymers; Salt removal; Permeability; BLOCK-COPOLYMER MEMBRANES; WATER DESALINATION; COMPOSITE MEMBRANES; HOLLOW-FIBER; SEAWATER DESALINATION; TRANSPORT-PROPERTIES; SHALE GAS; PERFORMANCE; ETHANOL; DEHYDRATION;
D O I
10.1016/j.memsci.2020.118460
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Pervaporation desalination has several advantages over competing desalination technologies, most notably an ability to select for or against volatile organic compounds and the ability to process high salinity feeds at a low transmembrane pressure. Pervaporation has not been commercialized for desalination applications because of its energy intensity. However, emerging processes such as hydraulic fracturing produce high total dissolved solids (>30-45 g L-1) byproduct streams that exceed the operational limits of traditional reverse osmosis and could be treated by pervaporation. Here, we demonstrate free-standing pervaporation membranes with excellent permeance and high salt removal based on a partially sulfonated pentablock terpolymer with the tradename Nexar (TM). Pervaporation membranes were easily cast from this material with desalination performances comparable or superior to commercially available membranes. We found that the polymer degree of sulfonation and casting solvent polarity had a significant impact on the membranes' water uptake but only a modest impact on the pervaporation desalination performance. Membranes with a degree of sulfonation of 52% (2.0 meq g(-1) IEC) and a casting solution composed of 50 wt% n-propanol and 50 wt% toluene achieved a water flux of 3.32 kg m(-2) h(-1) (permeance 135 kg m(-2) h(-1) bar(-1)) with 99.5% salt removal in pervaporation from a 32 g L-1 sodium chloride feed solution at room temperature. We demonstrated that dense, non-porous Nexar T pervaporation membrane permeance and salt separation performance were superior to commercial pervaporation membranes and equivalent to commercial membrane distillation membranes, which have much larger pores. This study demonstrates that commercially available sulfonated pentablock terpolymers are excellent membranes for pervaporation desalination because of their ease of casting and excellent performance.
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页数:9
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