Weschayanwiwat Punjaporn, Kunanupap Onanong, Scamehorn John F
National Center of Excellence for Environmental and Hazardous Waste Management, Chulalongkorn University, Bangkok 10330, Thailand.
Chemosphere. 2008 Jul;72(7):1043-8. doi: 10.1016/j.chemosphere.2008.03.065. Epub 2008 Jun 2.
A novel separation technique known as an aqueous surfactant two-phase (ASTP) extraction is a promising method to remove organic contaminants from wastewater. When cationic and anionic surfactants are mixed at certain surfactant concentrations and compositions, the solution separates into two immiscible aqueous phases. One is the surfactant-rich and the other is the surfactant-dilute phase. The organic contaminants will solubilize into the surfactant aggregates and concentrate in the small volume surfactant-rich phase. The other phase contains only small amount of surfactants and contaminants as the treated water. Most ASTP studies have used nonionic surfactants above the cloud point. Mixtures of anionic and cationic surfactants can also exhibit aqueous-aqueous phase separation and can be used in the ASTP extraction process. The phase behavior and performance of ASTP extraction using cationic surfactant dodecyltrimethylammonium bromide (DTAB) and anionic surfactant alkyldiphenyloxide di-sulfonate (DPDS) to extract benzene from wastewater was investigated in batch experiments. It was found that phase separation only occurs over a narrow range of molar ratios of DTAB:DPDS from 1.6:1 to 2.4:1. In this study, a 2:1 molar ratio of DTAB:DPDS at which there is no net charge in the surfactant aggregates show the highest extraction efficiency and lowest critical micelle concentration value with greatest synergism (highest negative values of the micellar interaction parameter). At a total surfactant concentration of 50mM, the benzene partition ratio is 48 and 72% of the benzene is extracted into the surfactant-rich phase solution in a single stage extraction, which is superior performance compared to ASTP extraction using nonionic surfactants.
一种名为水相表面活性剂双相(ASTP)萃取的新型分离技术是一种从废水中去除有机污染物的很有前景的方法。当阳离子和阴离子表面活性剂在特定的表面活性剂浓度和组成下混合时,溶液会分离成两个互不相溶的水相。一个是富含表面活性剂的相,另一个是表面活性剂稀释相。有机污染物会溶解到表面活性剂聚集体中,并浓缩在小体积的富含表面活性剂的相中。另一相作为处理后的水仅含有少量表面活性剂和污染物。大多数ASTP研究使用高于浊点的非离子表面活性剂。阴离子和阳离子表面活性剂的混合物也可以表现出水-水相分离,并可用于ASTP萃取过程。通过分批实验研究了使用阳离子表面活性剂十二烷基三甲基溴化铵(DTAB)和阴离子表面活性剂烷基二苯醚二磺酸盐(DPDS)从废水中萃取苯的ASTP萃取的相行为和性能。发现相分离仅在DTAB:DPDS的摩尔比从1.6:1到2.4:1的窄范围内发生。在本研究中,DTAB:DPDS摩尔比为2:1时,表面活性剂聚集体中没有净电荷,显示出最高的萃取效率和最低的临界胶束浓度值,具有最大的协同作用(胶束相互作用参数的最高负值)。在总表面活性剂浓度为50mM时,苯的分配比为48,在单级萃取中72%的苯被萃取到富含表面活性剂的相溶液中,与使用非离子表面活性剂的ASTP萃取相比,这是优异的性能。