纳米Fe3O4磁性液体稳定性的研究

从理论上解析了磁性颗粒之间的相互作用对纳米磁性液体稳定性的影响 ,指出磁粒半径和浓度 ,表面活性剂的包覆是影响磁液稳定性的重要因素 .采用湿化学共沉淀法制备了纳米Fe3O4 磁性液体 ,经过TEM等手段的表征 ,证明平均粒径为 10nm ,稳定性良好 .实验研究了加料方式、搅拌速度、分散作用、表面活性剂包覆时机、包覆时间和加入量以及pH值诸多工艺因素对磁液稳定性的影响 ,并分析了这些因素的影响机制     

溅射法制备Ag/Ag2O超微粒子的分析

用Ｘ射线衍射、Ｘ射线光电子能谱、透射电子显微镜和差示扫描量热法对溅射法制备的Ａｇ超微粒子的晶体学结构、表面组成、微粒形态和热力学性质进行了分析。结果表明，所制备的微粒为内部为Ａｇ、表面为Ａｇ₂Ｏ的两相微粒，以及单一的Ａｇ₂Ｏ微粒，粒径在１０ｎｍ以上的微粒没有确定的外形，粒径在１０ｎｍ以下的微粒为球形。微粒有不同于块体金属Ａｇ的异常热效应。到４０天时，沉积在碳膜上的Ａｇ，Ａｇ₂Ｏ两相微粒有一部份还原形成了单一的金属Ａｇ超微粒子。 关键词：     

空间多普勒激光雷达海表面散射信号分析

为了验证受海表面风速驱动的海表面反射率模型和计算海表面信号进行零风速校准的精度,开展了激光雷达海表面散射信号强度和速度特征的分析。在强度特征信息方面,进行了海表面反射率仿真模型和机载激光雷达海面散射信号实测数据的对比,考虑激光水下散射,参考QuikSCAT的海表面风速大小,测量结果和模型曲线基本吻合。在速度特征方面,通过海表面运动波形的仿真和海表面速度信息的提取,考虑波面的垂直和水平运动,采用时间积分的海表面探测信号零风速校准误差小于0.2 m/s。     

阳离子表面活性剂对液相银纳米微粒吸收光谱的影响

粒径为20 nm的黄色银纳米微粒在400 nm处有一吸收峰,当加入阳离子表面活性剂(CS)的浓度较低时,A_{400 nm}减小,波长大于400 nm以上的吸收增大且体系的吸收峰发生红;当CS浓度较高时,波长大于400 nm以上的吸收减小,而在400 nm处的吸收增大,体系的吸收峰发生蓝移。研究表明这是由于CS与带负电荷的银纳米存在较强的疏水和静电作用而导致银纳米微粒形貌的改变所致。     

界面活性剂对Fe3O4磁性与穆斯堡尔谱的影响

测量了不同颗粒尺寸Fe₃O₄覆盖界面活性剂前后磁性、红外谱以及穆斯堡尔谱。实验结果表明界面活性剂与Fe₃O₄微粒表面为化学吸附,覆盖界面活性剂后在相同磁场下磁化强度有所下降,穆斯堡尔谱变得弥散,随着颗粒尺寸变小,穆斯堡尔谱内场减小,谱线变得更为弥散,实验结果可以用表面各向异性的理论进行解释。 关键词：     

AOT微乳体系中纳米银的可控合成及其紫外-可见光谱研究

在以琥珀酸二异辛酯磺酸钠(AOT)为表面活性剂、环己烷为连续相形成的W/O型微乳体系中,用增溶于微乳液水核中的AgNO₃为银源、水合肼为还原剂制备了纳米银溶胶,利用UV-Vis光谱分析了AgNO₃的浓度、AOT的浓度、还原剂的种类和水与表面活性剂的物质的量比(W)等参数对形成粒子数量及平均粒径的影响,为纳米银粒子的可控合成和纳米银的UV-Vis光谱解析提供了新的依据。研究表明,适当增大AgNO₃的浓度,有利于形成粒径较小的纳米银粒子;W值增大,形成粒子的平均粒径和粒子数量明显增加。和NaBH₄相比,水合肼在反胶束中的溶解性能较好,有利于微乳液反胶束中Ag+的还原。增大AOT的浓度,在一定范围内胶束对反应物的增溶能力增强,胶束的半径也相应减小,有利于形成数量较多、平均粒径较小的纳米银粒子。     

活性剂浓度分布对液膜排液过程的影响

针对含不溶性活性剂的垂直液膜排液过程,考虑分离压和表面黏度的作用,应用润滑理论建立液膜厚度、活性剂浓度和表面速度的控制方程组,分析初始活性剂浓度及梯度对排液过程的影响.结果表明：当液膜表面不含活性剂时,其排液历程很短,很快发生破断.当液膜表面添加活性剂时,可以延长液膜存续时间.而当液膜表面活性剂浓度较低时,其诱发的Marangoni效应不足以克服重力的排液作用,其形成的"黑膜"不能稳定存在.随活性剂浓度增大,液膜表面流动速度减小,液膜表面更加"坚固",所形成的"黑膜"非常稳定.当考虑初始活性剂浓度梯度时,其影响主要体现在减缓排液初期的表面速度.     

Enhancement in Magnetorheological Effect of Magnetorheological Elastomers by Surface Modification of Iron Particles

为了研制具有高磁流变效应的磁流变弹性体,从新的化学修饰的角度制备了各向异性的橡胶基磁流变弹性体. 阴离子表面活性剂、非离子表面活性剂和复合表面活性剂等三种不同类型的表面活性剂分别用于修饰铁颗粒. 使用力磁耦合动态测试仪测量磁流变弹性体的动态剪切模量,并计算材料的磁流变效应. 测试结果表明,当Span 80的含量为15%时,材料的相对磁流变效应可达到188%,除了表面活性外,Span 80的增塑效应也有利于相对磁流变效应的增加. 当使用具有强表面活性的复合表面活性剂修饰铁颗粒时,用量只需0.4%,便可使相对     

碳点/海藻酸复合荧光纤维的制备及应用

以超支化聚乙烯亚胺和柠檬酸为原料,采用水热合成法制备了荧光碳点,探究了碳点的荧光性能和对四环素和Fe³⁺的传感特性。通过PEI表面氨基修饰,在EDC/NHS催化作用下通过羧胺缩合接枝到海藻酸纤维表面,得到了具有蓝色荧光的碳点/海藻酸复合荧光纤维。通过扫描电镜、共聚焦荧光显微镜和万能拉伸仪表征了纤维的微观形貌、荧光特性和机械性能,探究了纤维的荧光稳定性和传感性能。     

稀土纳米发光材料的燃烧法制备及光谱性质

用燃烧法制备了不同粒径的La2O3:Eu3 纳米微粒,研究了影响La2O3:Eu3 纳米微粒大小的实验条件,发现粒径大小随甘氨酸(Gly)与稀土离子比例的增大而减小.制备的纳米微粒由谢乐公式计算的粒径尺寸为12～28 nm.测量了样品的高分辨光谱.运用激光选择激发,研究了光谱在不同发光中心上的变化,表面态对于这些变化起着主要作用.     

Fabrication and Properties of Gelatin/Chitosan Microspheres Loaded with 5-Fluorouracil

The use of microspheres as drug delivery vehicles for anticancer therapeutics has great potential to revolutionize the future of cancer therapy. The present paper describes the influence of process variables on the encapsulation and loading efficiency of 5-Fluorouracil (5-FU) in gelatin/chitosan (Gel/Cs) microspheres. The influences of preparation parameters, including the contents of the emulsifier Span-80, the cross-linking agent and 5-FU, and the stirring speed, on drug loading and encapsulation efficiency of the microspheres were investigated. The experimental results indicated that drug loading and encapsulation efficiency of microspheres increased with increasing concentration of the cross-linking agent; and then decreased when the concentration of the cross-linking agent was higher than 0.3 ml·g^?1 of Gel/Cs. Drug loading and encapsulation efficiency increased with increasing concentration of Span-80; they reached the maximum value when the concentration of the emulsifier was 0.012 g·ml^?1. The loading and encapsulation efficiency of the microspheres also increased with increasing stirring speed. In addition, drug loading and encapsulation efficiency increased with increasing concentration of 5-FU; however, the encapsulation efficiency decreased when the concentration of 5-FU was higher than 40 mg·ml^?1.     

Fabrication of silk sericin/alginate microparticles by electrohydrodynamic spraying technique for the controlled release of silk sericin

Silk sericin has been recently investigated for many biological roles. This study aimed to develop the new delivery system to control the release of silk sericin. The alginate microparticles encapsulating silk sericin were fabricated by electrospraying technique. Concentrations of silk sericin and alginate polyelectrolyte solutions were investigated. All microparticles had an average size of 264–284 μm and could entrap silk sericin with high entrapment efficiency (84–89%). The microparticles could deliver silk sericin in a rate-controlled manner. This study would show a promising controlled release application of silk sericin protein from alginate microparticles fabricated by the means of electrostatic forces.     

Influences of Process Variables on Size of Chitosan Microspheres

Chitosan microspheres, with a size range of 20–550 μm, were obtained by using an emulsification–coacervation method. The surface morphology and the structure of microspheres were characterized by scanning electron microscopy and X-ray diffraction. The effects of process variables, including stirring rate, chitosan concentration, emulsifier concentration, and cross-linker (glutaraldehyde) concentration, on the diameter of chitosan microspheres were investigated. The results showed that spherical microspheres, without aggregation phenomena and with a very smooth and uniform surface, were obtained when emulsifier concentration, chitosan concentration, stirring rate, and glutaraldehyde concentration were kept at 0.010–0.025 mL/mL, 0.05–0.20 g/mL, 800–2400 rpm, and 0.5–1.5% (v/v) respectively. The chitosan microsphere crystallinity degree decreased after cross-linking. The microsphere size increased with decreasing of stirring rate, emulsifier, and cross-linker concentration; however, the microsphere size increased with increase of chitosan concentration. This indicated that different diameters of chitosan microspheres can be achieved by controlling process variables.     

Imaging contrast effects in alginate microbeads containing trapped emulsion droplets

This study focuses on spherical microparticles made of cross-linked alginate gel and microcapsules composed of an oil-in-water emulsion where the continuous aqueous phase is cross-linked into an alginate gel matrix. We have investigated the use of these easily manufactured microbeads as contrast agents for the study of the flow properties of fluids using nuclear magnetic resonance imaging. Results demonstrate that combined spin-spin (T(2)) relaxation and diffusion contrast in proton NMR imaging can be used to distinguish among rigid polymer particles, plain alginate beads, and alginate emulsion beads. Multi-echo CPMG spin-echo imaging indicates that the average spin-lattice (T(1)) and spin-spin (T(2)) relaxation times of the plain alginate and alginate emulsion beads are comparable. Meanwhile, diffusion-weighted imaging produces sharp contrast between the two types of alginate beads, due to restricted diffusion inside the embedded oil droplets of the alginate emulsion beads. While the signal obtained from most materials is severely attenuated under applied diffusion gradients, the alginate emulsion beads maintain signal strength. The alginate emulsion beads were added to a suspension and imaged in an abrupt, annular expansion flow. The emulsion beads could be clearly distinguished from the surrounding suspending fluid and rigid polystyrene particles, through either T(2) relaxation or diffusion contrast. Such a capability allows future use of the alginate emulsion beads as tracer particles and as one particle type among many in a multimodal suspension where detailed concentration profiles or particle size separation must be quantified during flow.     

A novel polysiloxane-based polymer as a gel agent for gel–VRLA batteries

In this study, a novel polysiloxane-based gel agent (PSGA) was synthesized by using poly(dimethylsiloxane-co-alkylmethylsiloxane) and used as a gel agent for gel–valve-regulated lead–acid batteries. A PSGA was characterized by Fourier transform infrared, zeta meter, scanning electron microscopy, and energy-dispersive X-ray analysis. The electrochemical characterization of the gel system for the optimization of some parameters, such as concentration of gel agent, stirring rate, and agitation time, was conducted by cyclic voltammetric and electrochemical impedance spectroscopic analyses. The optimum concentration of the gel agent was determined as 6 wt% of the PSGA to form the best gel structure. The mechanical parameters related to the formation of a suitable gel structure were also investigated. The optimum stirring rate and agitation time were determined as 500 rpm and 2.5 h, respectively. The charge–discharge tests were applied to the gel system, and the highest capacity was determined in the PSGA-based gel system as 10 mAh at the end of the 100th cycle. The capacity of non-gelled system was the lowest.     

Invert sugar formation with Saccharomyces cerevisiae cells encapsulated in magnetically responsive alginate microparticles

Invert sugar (an equimolar mixture of glucose and fructose prepared by sucrose hydrolysis) is a very important food component. We have prepared magnetically responsive alginate microbeads containing entrapped Saccharomyces cerevisiae cells and magnetite microparticles which can be easily separated in an appropriate magnetic separator. The microbeads (typical diameter between 50 and 100 μm) were prepared using the water-in-oil emulsification process. The prepared microbeads containing yeast cells with invertase activity enabled efficient sucrose conversion. The biocatalyst was quite stable; the same catalytic activity was observed after one month storage at 4 °C and the microbeads could be used at least six times.     

Size Tunable Fabrication of Magnetic Alginate Microparticles Using Flow Focusing Microfluidics

The size tunable formulation of magnetic alginate microparticles (MAMs) using a 3D flow-focusing microfluidic device is reported. The droplet phase consists of iron oxide nanoparticles (IONPs) in an alginate solution and the continuous phase consists of fluorocarbon oils. The stability of IONP colloids in alginate and calcium ethylenediamine tetraacetic acid solutions using optical microscopy, dynamic light scattering, and zeta potential measurements is studied. These studies suggest that IONPs coated with polyethylene glycol (PEG) are most stable. MAMs using the PEG-coated IONP colloid are then formulated and it is studied how MAM the average size and coefficient of variance vary as a function of droplet and continuous phase flow rates and viscosities. Droplet and MAM size decrease when the carrier flow rate or viscosity increases, and droplet and MAM size increase when droplet flow rate or viscosity increases. Crosslinking and drying of droplets result in MAMs whose diameter is ≈44% less than the original droplets while maintaining a population coefficient of variance below 8%. Conditions are identified that enable fabrication of MAMs with diameters between 30 and 60 µm with coefficients of variance of ≈6–7%. These results may guide future work exploring the role of MAM size on various applications.     

Preparation of Daidzein microparticles through liquid antisolvent precipitation under ultrasonication

In this study, daidzein microparticles (DMP) were prepared using an improved ultrasound-assisted antisolvent precipitation method. Preliminary experiments were conducted using six single-factor experiments, and principal component analysis (PCA) was adopted to obtain the three staple elements of the ultrasonic power, solution concentration, and nozzle diameter. The response surface Box-Behnken (BBD) design was used to optimize the level of the above factors. The optimal preparation conditions of the DMP were obtained as follows: the flow rate was 4 mL/min, the concentration of the daidzein solution was 16 mg/mL, the ratio of antisolvent to solvent (liquid-to-liquid ratio) was 9, the nozzle diameter was 300 μm, the ultrasonic power was 180 W (665 W/L), and the system speed was 760 r/min. The minimum average particle size of DMP was 181 ± 2 nm. The properties of daidzein particles before and after preparation were analyzed via scanning electron microscopy, X-ray diffraction analysis, Differential scanning calorimetry and Fourier transform infrared spectroscopy, no obvious change in its chemical structure was observed, but crystallinity was reduced. Compared with daidzein powder, DMP has a higher solubility and stronger antioxidant capacity. The above results indicate that the improved method of ultrasonication combined with antisolvent can reduce the size of daidzein particles and has a great potential in practical production.     

Ultrasound assisted enzyme catalyzed transesterification of waste cooking oil with dimethyl carbonate

This work reports the production of biodiesel with waste cooking oil and dimethyl carbonate in solvent free system through transesterification by immobilized enzyme (Novozym 435) under the influence of ultrasound irradiation. The experiments were conducted in an ultrasonic water bath under three different conditions i.e. ultrasonic irradiation (UI) without stirring, UI coupled with stirring and only stirring to compare their overall effects on fatty acid methyl esters (FAME) conversion. As compared with the conventional stirring method, where FAME conversion was 38.69% at 4 h, the UI without stirring significantly enhanced the conversion of enzymatic transesterification to 57.68% for the same reaction time. However the reaction rate was further increased under the condition of ultrasonication coupled with stirring and resulted into higher conversion of 86.61% for the same reaction time. Effects of reaction parameters, such as temperature, ratio of DMC/oil, speed of agitation and enzyme loading on the conversion were investigated. Furthermore, repeated use of Novozym 435 showed gradual decline in both conversion as well as enzyme activity.     

干凝胶粒子物性对空心玻璃微球炉内成球过程的影响

为实现干凝胶法制备惯性约束聚变靶用空心玻璃微球(HGM)炉内成球工艺过程的有效控制,从数值模拟和工艺实验两个方面研究了干凝胶粒子直径、比热容、发泡剂质量分数和辐射吸收系数对干凝胶粒子炉内成球过程及最终HGM性能参数的影响。结果表明,随着干凝胶粒子直径和/或比热容的增大,干凝胶粒子在吸热封装阶段的升温速率显著降低,在炉内成球过程各工艺阶段的停留时间快速下降,尤其是在精炼阶段的停留时间急剧缩短。降低干凝胶粒子的比热容和/或提高干凝胶粒子的发泡剂质量分数,HGM的直径和壁厚均匀性增大,高质量空心球的比例也相应提高。干凝胶粒子的辐射吸收系数变化对炉内成球过程几乎没有影响。