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81.
利用扫描电镜、热失重-红外、元素分析、低温氮吸附等技术和化学手段对聚羧酸基FFC-1离子交换纤维的结构与性能特点等进行了系统研究.结果表明:FFC-1离子交换纤维为含适量酰肼类交联键的聚羧酸(钠)型离子交换材料,外比表面积大和传质距离短是其反应动力学性能优异的主要原因,FFC-1纤维具有良好的化学与热稳定性。在5mol/L硫酸、硝酸、盐酸和2mol/L氢氧化钠溶液中浸泡,交换容量未见明显降低。但过氧化氢溶液对其功能基有明显破坏,CO2为FFC-1纤维在高温区间(300℃~350℃)的主要分解产物。 相似文献
82.
Ga^3+的新萃取体系的界面特性和胶团化作用研究 总被引:1,自引:0,他引:1
研究了Ga~(3+)协萃体系(Ga~(3+)-D_2EHPA-H_2MPA-正十二烷-H_2SO_4)的界面吸附和胶团形成热力学,发现该萃取体系中[H_2MPA]影响D_2EHPA和H_2MPA的界面吸附性质。在中、高[H_2MPA]范围内D_2EHPA与H_2MPA的界面吸附行为相反,D_2EHPA的存在也影响H_2MPA的界面吸附行为。研究了界面张力与各因素关系的数学模型,并获得某些胶团形成和界面吸附特性的物化参数。 相似文献
83.
聚合物共混物脆韧转变性能研究 Ⅲ.分散相形态参数之间的关系 总被引:4,自引:2,他引:4
为了研究形态(特别是分散状态)对聚合物共混物韧性的影响,建立了准网络形态模型,定义了分散相分布系数(ξ,0<ξ1),并给出其物理意义,推导了基体层厚度的计算公式,研究了形态参数的变化对基体层厚度的影响.对于常见的无规形态,ξ≈1.对于准网络形态,ξ<1,并且不是常数.计算结果表明,减小ξ和分散相粒径及其分布、增大其体积分数有利于减小基体层厚度.从理论上证明了准网络形态比无规形态更有利于减小基体层厚度. 相似文献
84.
Monodisperse poly(methyl methacrylate) (PMMA) particles containing various concentrations of stearyl methacrylate (SMA) were prepared, and a liquid crystal (LC) was swollen into the particles using a solute co-diffusion method (SCM). Phase separation behaviors between the polymer and LC were monitored by utilizing an optical and a polarized microscope (OM/POM). The monodisperse LC microcapsules were then applied to a polymer-dispersed liquid crystal (PDLC), and the electro-optical properties were investigated. As a result, the threshold and driving voltages were improved when the SMA content increased. The long alkyl chains of SMA in the capsules should exist at the interface of the LC and polymer resulting in an enhancement of phase separation between the polymer and LC, which largely influences the electro-optical properties of PDLC. 相似文献
85.
Taking soil colloid and hydrated silica (quartz sand) as the experimental material, the comparative study has been made on the kinetics of ion diffusion and ion exchange in charged colloid and charged coarse disperse systems. The results showed that ion exchange kinetics in the two systems conform to the kinetic law of ion diffusion. Besides, through this comparative study on the kinetics of ion exchange and ion diffusion, a method has been advanced theoretically to estimate the quantity of adsorbed ion that is located in the inner of the Helmholtz layer. As far as hydrated silica is concerned , there were about 33 per cent of the total adsorbed quantity of Mg2+that were located in the inner of the Helmholtz layer under the given experimental conditions, bu tfor soil colloid the percentage was only 7.5. 相似文献
86.
S. Shen E. D. Sudol M. S. El-Aasser 《Journal of polymer science. Part A, Polymer chemistry》1994,32(6):1087-1100
The mechanism for the formation of micron-size polymer particles in the dispersion polymerization of methyl methacrylate was investigated by applying dynamic light scattering to monitor the evolution of the average particle size in the early stages of the polymerization. In addition, the contributions of physically adsorbed stabilizer and graft copolymer were evaluated by measuring the bound, unbound (adsorbed), and free stabilizer, and by determining the amount of added stabilizer required in seeded dispersion polymerizations. Twenty nanometer particles (termed nuclei) were the smallest particles detected and are considered to be formed by aggregation of growing polymer chains precipitating from solution as they exceed their critical chain length. Aggregation of these nuclei with themselves and their aggregates continues until mature and stable particles are formed. This occurs when sufficient stabilizer occupies the particle surface which includes both the polymeric stabilizer [poly(vinylpyrrolidone)] and its graft copolymer which is created in situ. The effects of process variables are discussed based on this mechanistic picture of the dispersion polymerization process. © 1994 John Wiley & Sons, Inc. 相似文献
87.
用自制的带甲基侧基的环氧树脂(TMBP)作为界面增容剂, 从拉伸性能、键合胶含量、动态性能、扫描电镜和流变性能等方面, 研究了TMBP对炭黑在丁苯橡胶中分散度的影响, 并与市售通用双酚A型环氧树脂(E-51)和橡胶工业常用软化剂邻苯二甲酸二辛酯(DOP)进行了比较. 结果表明, 带甲基侧基的环氧树脂TMBP在提高炭黑分散性方面的效果远比E-51好, 其作用模式具有典型的增容特性. 相似文献
88.
A Taylor dispersion tube has been used to measure mutual diffusion in aqueous solutions of glycine hydrochloride at 25°C and concentrations from 0.0005 to 0.5 M. Analysis of the dispersion profiles shows that the diffusion of glycine hydrochloride (GlyHCl) produces a subtantial additional flow of hydrochloric acid that is liberated by the dissociation: GlyH+ + Cl- Gly + H+ + Cl-. Diffusion in this system is, therefore, a ternary process described by the equations J
1(GlyHCl) = – D
11C
1 – D
12C
2 and J
2(HCl) = –D
21C
1 – D
22C
2 for the coupled fluxes of total glycine hydrochloride (1) and hydrochloric acid (2) components. The ratio D
21/D
11 of measured diffusion coefficients indicates that up to two moles of HCl are cotransported per mole of GlyHCl. Although protonated glycine diffuses with relatively mobile Cl– counterions, the main diffusion coefficient of glycine hydrochloride, D
11, is lower than or nearly identical to the diffusion coefficient of aqueous glycine. A model for the diffusion of protonated solutes is developed to interpret this result and the large coupled flows of HCl. Diffusion coefficients are also reported for the aqueous hydrochlorides of 3- and 4-aminobenzoic acids. 相似文献
89.
Introduction Inorganic oxide films have attracted a lot of interest in the last several decades. Among them, silicon dioxide films are widely used in modern microelectronics, optics and mechanics. This material has been grown by various methods including thermal oxidation, chemical vapor phase deposition, plasma-enhanced chemical vapor phase deposition, and so on.1,2 Recently, Nagayama et al.3 have reported that SiO2 thin films could be produced by a new chemical method of liquid phase depos… 相似文献
90.
Effect of the type and number of high-speed impellers installed on a common shaft on the power characteristics was investigated
in water and glucose solutions of different concentration. Different configurations of the Rushton or Smith turbines, pitched
blade turbines, propeller, and A 315 impeller were tested. Measurements of power consumption were carried out within the transitional
and turbulent regime of the fluid flow using the strain gauge method. Baffled agitated vessels with inner diameter of 0.288
m and 0.634 m were used for the experiments. Liquid height in the vessels was equal to the vessel diameter or it was twice
higher. The relative power consumption was compared for different configurations of the impellers.
Presented at the 33rd International Conference of the Slovak Society of Chemical Engineering, Tatranské Matliare, 22–26 May
2006. 相似文献