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Quaternary ammonium bearing hyper-crosslinked polymer encapsulation on Fe3O4 nanoparticles

机译:季铵含有超交联聚合物在Fe3O4纳米粒子上包封

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The Gibbs free energy involved in the transfer of ions from water to a hydrophobic medium with ion-exchange sites changes the selectivity pattern expected from the electrostatic interactions. Oxyanions are less hydrated and, therefore, their exchange with more hydrated anions at the ion-exchange sites of a hydrophobic matrix in contact with aqueous solution is energetically more favorable. This gives rise to a possibility of separating the highly toxic monovalent oxyanions such as HCrO _(4) ~(?) , MnO _(4) ~(?) , TcO _(4) ~(?) and ClO _(4) ~(?) etc. by the Gibbs free energy of the transfer controlled anion-exchange process. In the present work, hydrophobic anion-exchange polymer encapsulation was anchored on Fe _(3) O _(4) particles by a simple and reproducible method for studying the selectivity pattern. The choice of Fe _(3) O _(4) nanoparticles (NPs) as the host matrix was based on their higher dispersion, larger surface area, and easy retrieval using an external magnetic field that is best suited for treating a large volume of an aqueous stream and developing sustainable technology. The anion-exchange polymer encapsulation was formed by first coating Fe _(3) O _(4) NPs with (3-aminopropyl)triethoxysilane, and subsequently reacting these precursor particles in a sequence with poly(vinylbenzyl chloride) (PVBCl), 1,4-diazabicyclo[2.2.2]octane (DABCO), and 1,8-dibromooctane (DBO). Each step involved in the chemical treatments was monitored by C, H and N analyses. Energy dispersive spectroscopy (EDS) and Fourier transform infrared spectroscopy (FTIR) were used to confirm the expected chemical structure of the encapsulation on the Fe _(3) O _(4) NPs. This sequence of chemical treatments resulted in the formation of hyper-crosslinked, hydrophobic, and high fixed positive charge density polymer encapsulation on the Fe _(3) O _(4) NPs. The analyses of the images obtained from field emission scanning electron microscopy (FE-SEM) and transmission electron microscopy (TEM) indicated that the sizes of the Fe _(3) O _(4) NPs were increased from 13 ± 3 nm to 33 ± 3 nm due to the formation of polymer encapsulation and inter-particle crosslinking. Although a very dilute solution and ultrasonication were used, there was a possibility of crosslinking between the particles. However, the thus encapsulated Fe _(3) O _(4) NPs retained their superparamagnetic properties having a reasonably good magnetic saturation (30 emu g ~(?1) ). The anion-exchange capacity was found to be 0.65 ± 0.03 meq g ~(?1) . The Fe _(3) O _(4) @PVB–DABCO–DBO particles exhibited a selectivity pattern corresponding to the Hofmeister series, i.e. the least hydrated anions were adsorbed preferentially. For example, the least hydrated representative TcO _(4) ~(?) anions adsorbed quantitatively in the Fe _(3) O _(4) @PVB–DABCO–DBO particles from aqueous solutions such as ground water, seawater, and 0.5 mol L ~(?1) HNO _(3) with efficiencies of 98%, 80% and 75%, respectively.
机译:在具有离子交换位点将离子转移到疏水介质的离子转移到疏水介质中的Gibbs自由能将预期的静电相互作用的选择性模式改变。氧气较低,因此它们在与水溶液接触的疏水基质的离子交换位点处具有更多的水合阴离子,能量更有利。这引起了分离高毒性的一价氧合如HCRO _(4)〜(α),MNO _(4)〜(α),TCO _(4)〜(?)和CLO _(4)的可能性〜(?)等。通过吉布斯的转移控制阴离子交换过程的自由能。在本作工作中,通过简单而可再现的方法来研究选择性模式,疏水阴离子 - 交换聚合物包封在Fe _(3)O _(4)颗粒上锚定。作为宿主基质的Fe _(3)O _(4)纳米颗粒(NPS)的选择基于其更高的色散,较大的表面积,并且使用最适合处理大量的外部磁场,易于检索水流和发展可持续技术。通过第一涂布Fe _(3)O _(4)NPS与(3-氨基丙基)三乙氧基硅烷的第一涂布Fe _(3)O _(4)NPS形成阴离子 - 交换聚合物包封,并随后将这些前体颗粒以聚(乙烯基苄氯苄氯)(PVBCL)的序列反应,1 ,4-二氮杂双环[2.2.2]辛烷(DABCO)和1,8-二溴辛烷(DBO)。通过C,H和N分析监测化学处理中涉及化学处理的每一步。能量分散光谱(EDS)和傅立叶变换红外光谱(FTIR)用于确认FE _(3)O _(4)NPS上的包封的预期化学结构。这种化学处理序列导致在Fe _(3)O _(4)NPS上形成超交联,疏水和高固定的正电荷密度聚合物包封。从场发射扫描电子显微镜(Fe-SEM)和透射电子显微镜(TEM)获得的图像的分析表明FE _(3)O _(4)NP的尺寸从13±3nm增加到33由于聚合物包封和颗粒间交联的形成,±3nm。虽然使用了非常稀释的溶液和超声,但颗粒之间存在交联的可能性。然而,如此包封的Fe _(3)O _(4)NPS保留其具有合理良好磁饱和度的超顺磁性(30 emu g〜(α1))。发现阴离子交换能力为0.65±0.03 meq g〜(?1)。 Fe _(3)O _(4)@ PVB-Dabco-DBO颗粒表现出与Hofmeister系列相对应的选择性模式,即优选地吸附了最少的水合阴离子。例如,最少的水合代表性的代表性TCO _(4)〜(α)阴离子定量在Fe _(3)O _(4)℃的PVB-Dabco-DBO颗粒中,来自水溶液,如地面水,海水和0.5 Mol L〜(α1)HNO _(3)分别为98%,80%和75%的效率。

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