反渗透过程中双壁碳纳米管通水阻盐性能的分子动力学模拟

采用分子动力学模拟方法, 探究了非常规双壁碳纳米管(DWCNT)在反渗透过程中, 不同内外管间距对管道内水分子与盐离子运动行为的影响. 本文采用0.5 mol·L^-1氯化钠水溶液模拟海水, 内管始终采用CNT(8,8)型, 并对盐水层施加恒力模拟反渗透压. 重点考察盐离子数量分布与通水情况, 计算水分子平均力势, 并分析水分子氢键寿命与偶极矩分布. 结果表明, 管间距不仅影响上述各项性质, 还会改变盐离子与水分子在碳管中的渗透特性. 模拟结果显示, 小尺寸DWCNT可以有效实现盐水分离但水通量较小, 大尺寸DWCNT的水容量较大但阻盐效率不高, 而中尺寸DWCNT (即: 管间距为0.815 nm)则具有最佳的通水阻盐性能. 本文试图从分子层面揭示了DWCNT通水阻盐机理, 并为人们设计新型海水淡化渗透膜提供理论指导.     

以荷电化碳纳米管构筑正渗透膜用于海水淡化的分子动力学模拟

受传统膜科学中分离膜的荷电化可提升膜盐水分离效能的启发,在前期工作基础上尝试以荷电化碳纳米管CNT(8,8)为水通道仿生构筑正渗透膜,利用分子动力学模拟的方法研究水分子在膜中的传递行为.模拟中,以0.5mo·lL-1氯化钠溶液模拟海水,1mo·lL-1的氯化镁溶液为汲取液,考察不同电量电荷修饰对碳纳米管正渗透膜中水分子密度分布、扩散系数以及水通量的影响.结果显示,电荷修饰对碳纳米管中水分子的密度分布和扩散速率以及水通量影响较显著,当碳纳米管管口荷电量为-0.3e时,碳纳米管膜可获得最大水通量.     

受限于纳米碳管中的乙醇分子的结构和扩散的分子模拟研究

利用分子模拟研究了常温常压下受限于(8,8) (管径1.081 nm)和(15,15) (管径 2.035 nm)单壁纳米碳管中的乙醇分子. 对受限分子的径向密度分布和氢键等静态性质以及扩散性质进行了分析. 结果显示在管内乙醇分子的平均氢键数目和主体相一致. 乙醇分子在(8,8)碳管内具有高度有序的结构, 而在(15,15)碳管内由于空间的增大导致结构有序度的降低, 其中分子取向已呈随机分布. 进一步对扩散系数的分析发现, 在管内乙醇分子的轴向扩散系数低于主体相, 特别在(8,8)碳管内乙醇分子几乎丧失了轴向扩散能力.     

手性和尺寸对受限于单壁碳纳米管内的硝基甲烷热解反应的影响

采用组合的量子化学ONIOM(B3LYP/6-311++G**:UFF)方法, 研究了不同直径的扶手椅型(CNT(5,5)、CNT(6,6)、CNT(8,8))和锯齿型(CNT(9,0)、CNT(10,0)、CNT(11,0))单壁碳纳米管(CNTs)的限制作用对硝基甲烷分子结构和热解反应的影响. 分子结构分析表明, 与单体硝基甲烷相比, 受限于直径较小的CNT(5,5)和CNT(9,0)碳纳米管内的硝基甲烷构型发生扭转, Cs对称性消失, C—N键长略微缩短; 而受限于CNT(6,6)、CNT(8,8)、CNT(10,0)和CNT(11,0)内的硝基甲烷结构变化不明显. 热解势能面计算发现, 与硝基甲烷单体的热解是一个无过渡态的解离过程明显不同: 硝基甲烷在CNT(5,5)和CNT(9,0)碳纳米管内沿C—N键的解离经历过渡态结构, 所需克服的活化能比单体的解离能分别下降了约71和58 kJ·mol-1; 在CNT(6,6)和CNT(10,0)碳纳米管内, 硝基甲烷的热解活化能略有下降; 而在直径较大的CNT(8,8)和CNT(11,0)碳纳米管内, 热解活化能基本不变. 研究结果表明, 直径小的碳纳米管的限制作用对硝基甲烷热解活化能影响显著, 碳纳米管的手性对硝基甲烷热解反应影响不明显.     

分子动力学模拟研究纳米碳管中甲醇-水混合溶液的结构与输运性质

利用分子动力学模拟方法,对比考察了平衡条件、外压作用、梯度电场作用下,摩尔比为1:1的甲醇-水混合溶液在纳米碳管(CNT)中的静态结构以及输运行为.研究发现:在平衡体系与外压作用下,纳米碳管内甲醇与水呈现出明显的不混溶现象,甲醇主要分布于管壁附近,水分子主要分布于纳米碳管轴心附近;而在梯度电场作用下,纳米碳管由疏水性向亲水性转变,更多的水分子分布于管壁,导致纳米碳管内甲醇-水的不混溶现象消失.另一方面,在外压作用下,纳米碳管内甲醇与水呈现单向移动;而在梯度电场下,甲醇与水呈现快速的双向移动,其流通量较相应外压作用体系高出近一个数量级,但由于双向的流通量大小相近,导致净流通量与外压作用下的净流通量差异不大.     

碳纳米管表面羧基对纳米RuO2颗粒的分散作用

采用硝酸氧化方法对多壁碳纳米管(CNT)的侧壁进行修饰,得到表面羧基含量可控的CNT,并进一步考察了碳管表面基团分布与纳米RuO2催化剂在CNT上的分散度及催化氧化活性之间的关系.以多齿羧酸配体作为稳定剂,合成了RuO2和IrO2纳米颗粒水溶胶,并通过改变配体的种类及数最对纳米颗粒团聚体粒径进行调控.研究结果表明,羧酸配体和碳管表面的羧基均有助于纳米氧化物颗粒的分散.     

分子动力学模拟研究纳米碳管中甲醇-水混合溶液的结构与输运性质

利用分子动力学模拟方法,对比考察了平衡条件、外压作用、梯度电场作用下,摩尔比为1：1 的甲醇-水混合溶液在纳米碳管（CNT）中的静态结构以及输运行为. 研究发现：在平衡体系与外压作用下,纳米碳管内甲醇与水呈现出明显的不混溶现象,甲醇主要分布于管壁附近,水分子主要分布于纳米碳管轴心附近;而在梯度电场作用下,纳米碳管由疏水性向亲水性转变,更多的水分子分布于管壁,导致纳米碳管内甲醇-水的不混溶现象消失. 另一方面,在外压作用下,纳米碳管内甲醇与水呈现单向移动;而在梯度电场下,甲醇与水呈现快速的双向移动,其流通量较相应外压作用体系高出近一个数量级,但由于双向的流通量大小相近,导致净流通量与外压作用下的净流通量差异不大.     

纳米碳与石墨碳复合材料的电化学性能

在天然石墨(NG)中掺杂不同比例的碳纳米管(CNT)得到纳米碳与石墨碳的复合材料.电化学测试结果表明,在NG中掺杂质量分数为10%的CNT所得复合材料的电化学性能最好.经过20次充放电循环,该复合材料的放电容量比同样条件下的石墨提高15.9%.纳米碳管的中空式结构和不易塌陷的特点使复合材料的充放电容量和循环稳定性明显提高.     

纳米多孔结构镍基复合膜电极的电化学法制备及其电容特性

通过对电沉积法得到的Ni-Cu合金镀层进行电化学去合金化处理, 制备了纳米多孔结构金属镍膜. 采用循环伏安法对多孔金属镍膜在1 mol·L^-1 KOH溶液中进行阳极氧化处理, 获得了纳米多孔结构的镍基复合膜电极. 应用扫描电子显微镜(SEM)、X射线衍射(XRD)、X射线光电子能谱(XPS)和电化学技术对所制备的膜电极的物理性质及赝电容特性进行了表征. SEM、XRD和XPS的测试结果表明, 所制备的纳米多孔结构镍基复合膜由Ni、Ni(OH)₂和NiOOH组成. 电化学实验结果显示, 该复合膜在20 A·g^-1的充放电电流密度下, 给出了578 F·g^-1的初始比电容; 在1000次充放电循环后, 它的比电容值为544 F·g^-1, 电容保持率为94%. 纳米多孔结构有利于KOH电解液的渗透, 从而促进反应物种在电极内部的传输; 纳米多孔的金属镍基体可以提高Ni(OH)₂膜的电子导电性; 纳米大小的Ni(OH)₂颗粒能够缩短质子的固相扩散路径. 上述因素是所制备的纳米多孔结构镍基复合膜电极具有优异赝电容特性的主要原因.     

纳米受限下溶质水化结构的分子模拟

利用分子动力学模拟研究了五种不同种类的溶质分子(K+, Mg2+, Cl-, K-和K0)在直径为0.60-1.28 nm的纳米碳管内的水化结构. 模拟结果揭示了单电荷溶质、双电荷溶质和中性溶质在受限条件下具有不同的水化行为. 单价溶质的配位数只有在直径不大于0.73 nm的纳米碳管内才会明显减少. 和带有电荷的溶质不同, 中性溶质的配位数对纳米碳管直径的改变非常敏感, 并且随着管径的减小而迅速减少. 模拟结果还表明带单价正电荷的溶质(K+)第一配位层水分子的取向结构会随着纳米碳管直径的改变发生变化, 而其他溶质配位层取向结构在本文所涉及的纳米碳管内都几乎和体相中一致. 在直径大于1.0 nm的纳米碳管中, K+的配位层取向结构有序度随着管径的减小而单调下降, 但是在直径小于1.0 nm的纳米碳管中, 随着碳管管径的减小而迅速上升. 在两个最窄的纳米碳管内, 其结构有度甚至高于体相. 双电荷溶质的水化结构在本文所研究的碳管直径范围内和体相完全一致, 即使在直径只有0.6 nm的碳管内也无任何改变.     

Chitosan‐modified graphene oxide as a modifier for improving the structure and performance of forward osmosis membranes

Chitosan (CS) with good hydrophilicity and charged property was used to modify graphene oxide (GO), the obtained GO‐CS was used as a novel modifier to fabricate thin film composite forward osmosis (FO) membranes. The results revealed that the amino groups on CS reacted with carboxyl groups on GO, and the lamellar structure of the GO nanosheets was peeled off by CS, resulting in the reducing of their thicknesses. The GO‐CS improved the hydrophilicity of polyethersulfone (PES) substrate, and their contact angles decreased to 64° with the addition of GO‐CS in the substrate. GO‐CS also increased the porosity of the substrate and surface roughness of FO membrane, thereby optimizing the water flux and reverse salt flux of FO membrane. The average water flux of the FO membrane reached the optimal flux of 21.34 L/(m² h) when GO‐CS addition was 0.5 wt%, and further addition of GO‐CS to the substrate would decrease the water flux of FO membrane, and the reverse salt flux also decreased to the lowest value of 2.26 g/(m² h). However, the salt rejection of the membrane increased from 91.4% to 95.1% when GO‐CS addition increased from 0.5 to 1.0 wt% under FO mode using 1 mol/L sodium chloride (NaCl) solution as draw solution (DS). In addition, high osmotic pressure favored water permeation, and at the same concentration of DS, magnesium chloride (MgCl₂) exhibited better properties than NaCl. These results all suggested that GO‐CS was a good modifier to fabricate FO membrane, and MgCl₂ was a good DS candidate.     

木质素磺酸钠改性聚砜膜的制备及其在正渗透膜中的应用

采用木质素磺酸钠作为亲水添加剂,通过浸没沉淀相转化法制备了木质素磺酸钠共混改性聚砜膜,以改善聚砜膜的亲水性,并用作正渗透膜的支撑层,以降低内浓差极化效应.利用扫描电子显微镜、衰减全反射傅里叶变换红外光谱仪、水接触角仪等研究了不同木质素磺酸钠添加量对聚砜膜的结构和表面性质的影响.结果表明,添加木质素磺酸钠后,聚砜膜的指状孔变得规整且狭长.水接触角实验证实添加木质素磺酸钠能改善聚砜膜的亲水性,当木质素磺酸钠含量为0.4 wt%时,聚砜膜的表面水接触角可降低至65°.正/反渗透测试装置分别用于表征正渗透膜的传质性质和结构参数.结果表明,以0.4 wt%木质素磺酸钠改性聚砜膜为支撑层的正渗透膜的水渗透性能(A=3.12×10~(-5) LMH×Pa~(-1))优于纯聚砜基底正渗透膜(0.76×10~(-5)LMH×Pa~(-1)),而且前者的结构参数(S=2010mm)远小于后者(3450mm),说明木质素磺酸钠改性聚砜膜有效弱化了正渗透膜的内浓差极化效应.     

Channel regulation of TFC membrane with hydrophobic carbon dots in forward osmosis

Zero-dimensional carbon dots have emerged as important nanofillers for the separation membrane due to their small specific size and rich surface functional groups. This study proposed a strategy based on hydrophobic carbon dots (HCDs) to regulate water channels for an efficient forward osmosis (FO) membrane. Thin-film composite (TFC) membranes with superior FO performance are fabricated by introducing HCDs as the nanofiller in the polyacrylonitrile support layer. The introduction of HCDs promotes the formation of the support layer with coherent finger-like hierarchical channels and micro-convex structure and an integrated polyamide active layer. Compared to the original membrane, TFC-FO membrane with 10 wt% HCDs exhibits high water flux (15.47 L m⁻² h⁻¹) and low reverse salt flux (2.9 g m⁻² h⁻¹) using 1 mol/L NaCl as the draw solution. This improved FO performance is attributed to the lower structural parameters of HCDs-induced water channels and alleviated internal concentration polarization. Thus, this paper provides a feasible strategy to design the membrane structure and boost FO performance.     

聚多巴胺/聚乙烯亚胺共沉积中间层增强薄膜复合正渗透膜性能

以聚多巴胺/聚乙烯亚胺(PDA/PEI)共沉积于三醋酸纤维素(CTA)多孔支撑膜表面形成中间层,再结合界面聚合法获得聚酰胺薄膜,构建了PDA/PEI共沉积中间层改性薄膜复合(TFC)正渗透(FO)膜.通过傅里叶变换衰减全反射红外光谱法、扫描电子显微镜、原子力显微镜、溶质截留法、水接触角仪等研究了PDA/PEI共沉积中间层对CTA膜和TFC膜的表面结构和性质的影响.研究结果表明,PDA/PEI共沉积使得CTA膜表面变得更为平滑,表面孔径减小至(30.0±4.1) nm,且表面孔径分布趋于均一.同时,在PDA/PEI共沉积改性CTA膜表面界面聚合得到的聚酰胺层呈现出更均匀的叶片状结构和优异的亲水性.基于此,具有PDA/PEI共沉积中间层的TFC正渗透膜显著提高了水通量(FO模式:(7.1±2.3) L/(m^2·h)),较空白TFC膜提升了57.6%.同时,中间层改性TFC膜具有更低的反向盐通量(FO模式:1.4±0.1 g/(m^2·h))和"净盐通量"(FO模式:(0.2±0.06) g/L),与空白TFC膜相比分别下降了83.9%和90.6%.说明PDA/PEI共沉积中间层不仅能有效提升TFC正渗透膜的水渗透性,而且大幅提升了膜的截盐性和渗透选择性.     

径向电场对纳米管中水分子通量的影响

水分子在纳米通道中的运动对于生命活动、纳米器件的设计等都有着重要的意义. 现在已经证实, 在(6,6)的碳纳米管中, 水分子会以单分子水链的形式协同通过碳纳米管. 但是如何控制水分子的流量仍然是一个困难的课题. 本文研究了在径向电场作用下, 碳纳米管中水分子通量的变化趋势和碳纳米管的开关行为.发现在碳纳米管两端存在200 MPa的压力差时, 电场强度从1 V·nm^-1增加到3 V·nm^-1, 水分子通量线性减小. 当径向电场强度增加到3 V·nm^-1时, 碳纳米管处于关闭状态, 水分子无法通过碳纳米管. 进一步, 我们发现水偶极与碳纳米管管轴夹角的平均值的概率分布和翻转频率都与水分子在纳米管中的个数有很大关系.     

Novel nanocomposite pervaporation membranes composed of poly(vinyl alcohol) and chitosan-wrapped carbon nanotube

Novel nanocomposite membranes (PVA–CNT(CS)) were prepared by incorporating chitosan-wrapped multiwalled carbon nanotube (MWNT) into poly(vinyl alcohol) (PVA). To further explore the intrinsic correlation between pervaporation performance and free volume characteristics, molecular dynamics simulation was first introduced to qualitatively analyze the contribution of carbon nanotube incorporation on improving free volume characteristics of the nanocomposite membranes. Secondly, the pervaporation performance of PVA–CNT(CS) nanocomposite membranes was investigated using permeation flux and separation factor as evaluating parameters. For benzene/cyclohexane (50/50, w/w) mixtures at 323 K, permeation flux and separation factor of pure PVA membrane are only 20.3 g/(m² h) and 9.6, respectively, while the corresponding values of PVA–CNT(CS) (CNT content: 1%) nanocomposite membrane are 65.9 g/(m² h) and 53.4. In order to explain the simultaneous increase of permeation flux and separation factor, as well as to check the calculation reliability of molecular dynamics simulation, positron annihilation lifetime spectroscopy (PALS) analysis was employed.     

Study on preparation and performances of cellulose acetate forward osmosis membrane

Cellulose acetate (CA) forward osmosis (FO) membranes were prepared via a phase inversion process. CA was used as membrane material for FO. Acetone and 1,4-dioxane were employed as solvent. Polyvinylpyrrolidone (PVP), maleic acid, and methanol were applied as additives. An orthogonal experiment was performed to optimize the ratio of every component in the casting solution. The membrane with best performance was selected to concentrate an anthocyanin solution. Saturated sucrose solution (about 60°Brix) was fit for using as draw solution in the concentration experiment. Water flux, porosity, and rejection rate were measured to evaluate the membrane properties. Reverse water rinsing was used in cleaning membrane that was fouled by anthocyanin solution. Results showed that under membrane thickness of 100 μm, coagulation temperature at room temperature, and evaporation time of 30 s, the optimum components in casting solution were 13% CA, 45% 1,4-dioxane, 31% acetone, 2% maleic acid, 3% PVP, and 6% methanol. In the concentration experiment, the prepared FO membrane showed water flux of 2.04 L m^?2 h^?1 and rejection rate of 98.61%. In the membrane cleaning experiment, the water flux of the FO membrane recovered 87.51% after rinsing for 1 h. The prepared membranes and previously published membranes were compared which showed the prepared membrane could significantly improve the rejection rate for anthocyanin solution.     

Nanofiltration-like forward osmosis membranes on in-situ mussel-modified polyvinylidene fluoride porous substrate for efficient salt/dye separation

Here, polyvinylidene fluoride (PVDF) membranes were fabricated via non-solvent induced phase separation (NIPS) using dopamine (DA) and polyethyleneimine (PEI) as the hydrophilic additives, which has a loose surface and somewhat improved hydrophilicity. Then nanofiltration (NF)-like thin-film composite forward osmosis (TFC FO) membrane with a loose polyamide (PA) active layer on the blend membrane was synthesized via the interfacial polymerization. The as-prepared NF-like TFC FO membrane exhibited a high water flux (J_w) of 29.98 L m⁻² h⁻¹ and a much low specific salt flux (J_s/J_w) of 0.018 g/L, when 0.6 M NaCl was used as draw solution (DS). It had a superior rejection of malachite green (99.6% ± 0.1%) and a low rejection of NaCl (27.4% ± 4.2%), when filtrated malachite green/NaCl mixture solution in active layer-facing draw solution (AL-FS) mode. The results provide new insights on the design and preparation of FO membranes of selective separation for dyes from salty water.     

Polybenzimidazole (PBI) nanofiltration hollow fiber membranes applied in forward osmosis process

For the first time, the potential of polybenzimidazole (PBI) nanofiltration membrane as a forward osmosis membrane has been investigated. PBI was chosen mainly because of its unique nanofiltration characteristics, robust mechanical strength and excellent chemical stability. The MgCl₂ solutions with different concentrations and other different salt solutions were employed as draw solutions to test the water permeation flux through the PBI membrane during forward osmosis. High water permeation flux and excellent salt selectivity were achieved by using the PBI nanofiltration membrane which has a narrow pore size distribution. Effects of membrane morphology, operation conditions and flowing patterns of two feed streams within the membrane module on water transport performance have been investigated. It may conclude that PBI nanofiltration membrane is a promising candidate as a forward osmosis (FO) membrane.