纳米壳聚糖修饰的开管毛细管电色谱柱的制备及对碱性蛋白质的分离

采用离子交联法制得纳米壳聚糖粒子溶液,通过静电吸附作用将其修饰于石英毛细管内表面形成涂层毛细管柱.通过场发射扫描电子显微镜观察到毛细管内壁有小丘状突起,表明纳米壳聚糖粒子已吸附于柱内层.检测了不同p H值下的电渗流变化趋势并与裸柱比较,结果显示修饰后的柱电渗流受到明显抑制,并在p H4.7的环境中能产生反向电渗流,该柱在不同p H值下电渗流的相对标准偏差(RSD)6%,日内、日间和柱间的RSD分别为1.46%,4.64%和14.43%,表明柱稳定性较好.通过分离3种中性物质甲苯、苯酚和硫脲考察了该柱的色谱行为,出峰顺序与其极性大小顺序一致,表明纳米涂层起到极性固定相的作用.用该柱成功分离了3种碱性蛋白质溶菌酶、细胞色素c和核糖核酸酶A,柱效分别为39481,42610和245373Plate/m,重现性良好,表明纳米涂层可有效抑制碱性蛋白质的吸附作用.     

Improved hydrogen evolution on glassy carbon electrode modified with novel Pt/cetyltrimethylammonium bromide nanoscale aggregates

A novel, cost‐effective, and simple electrocatalyst based on a Pt‐modified glassy carbon electrode (GCE), using cetyltrimethylammonium bromide (CTAB) as a cationic surfactant, is reported. Am‐phiphilic...     

共沸点存在的充分条件

以纯液体蒸气压和亨利系数为出发点,讨论了二组分气液相图存在共沸点的充分条件。结合纯液体蒸气压和亨利系数的物理意义,对共沸点存在的条件进行了说明。     

两种功能化纳米金粒子固酶电极的催化性能

以合成的4-巯基苯甲酸功能化纳米金粒子和聚乙烯基吡啶包覆纳米金粒子分别作为固酶载体,制备了2种新型固酶电极,在此基础上组装了2种酶燃料电池。采用电化学方法结合紫外可见分光光度法、透射电镜技术等手段研究了固酶载体的形貌,酶-载体间相互作用对电极表面固定酶分子的光谱学性质,酶-电极间直接电子迁移能力和催化底物反应性能的影响,进一步评估和比较了两种酶燃料电池的能量输出性能。实验结果表明：4-巯基苯甲酸功能化纳米金粒子固酶基电极可以实现酶-电极间的直接电子迁移而且对葡萄糖和氧气具有良好的催化性能(催化反应起始电位分别为-0.03和0.96 V,底物转化频率分别是1.3和0.5 s^-1),其催化性能的重现性、长期使用性能、酸碱耐受性和热稳定性良好,随着自组装固酶层数的增加,催化性能随之增强直至达到极限催化电流;电池性能测试结果表明4-巯基苯甲酸功能化纳米金粒子固酶基燃料电池的开路电压为0.88 V,最大输出能量密度：864.0 μW·cm^-2,长期使用性能优异(储存3 周后仍可达到最佳能量输出的80%以上)。     

Modeling of dynamics, heat transfer, and combustion in two-phase turbulent flows: 2. Flows with heat transfer and combustion

The objective of this part of the paper is to summarize the information concerning the authors' works in the field of simulation of two-phase gas-particle turbulent flows with heat transfer and combustion. A kinetic equation had been derived for the probability density function (PDF) of the particle velocity, temperature, and mass distributions in turbulent flows. This PDF equation is used for the construction of the governing conservation equations of mass, momentum, and heat transfer in the dispersed particle phase.The numerical scheme incorporates two-phase fluid dynamics, convective and radiative heat transfer, and combustion. The proposed models have been applied to the calculation of various particle-laden turbulent flows in jets, combustion and gasification chambers, and furnaces.     

Phase volume and size effects on the terminal relaxation of ABS melts

The dynamical viscoelasticity of ABS melts with different particle size was investigated at various levels of rubbery phase contents. The effects of the rubber are more pronounced in the terminal zone: a transition from viscoelastic liquid to viscoelastic solid behavior was observed which can be interpreted as a physical gelation occurring at a critical rubbery phase content. This critical content resulted in being smaller in the case of smaller particles. A quantitative explanation of the experimental findings was proposed in terms of the average interparticle distance and overlapping of the chains grafted onto the neighboring rubber particles. The gel-like transition appeared to correspond to an approximately constant level of grafted chains overlapping.Presented in part at the Symposium Recent Developments in Structured Continua, Montreal (Canada), 26–28 May 1993.     

h-ADAPTIVITY ANALYSIS BASED ON MULTIPLE SCALE REPRODUCING KERNEL PARTICLE METHOD

IntroductionAs one of the meshfree methods, multiple scale reproducing kernel particle method(RKPM)[1,2]bears, besides the common features of all meshfree methods, a uniqueinherent feature of multiresolution analysis by which the structural response can b…     

两相流PIV粒子图像处理方法的研究

本文在单相PIV技术的基础上研究了两相流动PIV图像处理方法，采用摸板匹配法和灰度加权标定法对两相粒子进行了识别、区分和标定，采用灰度互相关法对区分后的单相粒子图像进行了处理，应用基于以上方法编制的Windows应用软件，首先对由美国Minnesota大学复杂流动实验室提供的两相流动粒子图片进行了处理，通过对比分析可见，应用本文所采用的方法能对两相粒子进行有效的识别和区分，然后以搅拌槽内液固两相流场为例对此方法进行了应用。     

Filtration in a Porous Granular Medium: 2. Application of Bubble Model to 1-D Column Experiments

This paper describes the formulation of a quasi-1-D network model, referred to as the ‘bubble model’, and its application for simulating particle transport and filtration through a granular filter bed. The model comprises a series of homogeneous sites linked through bundles of cylindrical bonds that represent flow pathways through distributions of pores and pore throats. This model incorporates pore scale processes of particle sieving and infiltration are based on numerical simulations described in a companion paper. The modeling of infiltration is further refined based on detailed experimental observations and measurements of the filtration of a dilute suspension of acrylic particles through a column of glass beads reported by Yoon et al. (2005 Water Resour. Res., to appear). Their data distinguish (a) between the collection of particles on grain surfaces and at grain-to-grain contact points, and (b) between particles that are fully entrapped and those that are hindered (temporarily collected) and can later become detached. These effects are represented by two parameters that characterize the probability of attachment and are linked to the surface roughness of the grains; one that describes the minimum particle size that can be fully entrapped, and one that describes the detachment rate. These parameters can be readily calibrated from conventional measurements of effluent concentration and effluent particle size distribution. Detailed comparisons with the data reported by Yoon et al. show that the proposed bubble model is able to achieve reliable predictions of the spatial distribution of particles within the filter bed following phases of particle injection and washing.