高效液相色谱峰压缩中灵敏度增加值与峰压缩因子的关系研究

以从塔板理论得到的色谱流出曲线为基础,推导了高效液相色谱(HPLC)双流动相分离场中实现峰压缩时,峰压缩因子(峰压缩后的半峰宽与未进行峰压缩时的半峰宽的比值)和峰高表示的灵敏度变化(峰压缩后的峰高与未进行峰压缩时的峰高的比值)的关系,结果表明峰高表示的灵敏度增加值等于峰压缩因子的倒数.并用色氨酸、香豆素、苯和2-硝基酚在不同速率差实现堆积时的相关参数进行了验证.实验结果表明,这些化合物在各个峰压缩条件下的峰压缩因子倒数和实际灵敏度增加值相等,实验结果与理论推导结果一致.考察了该关系式在实际样品测定中的应用,结果表明灵敏度增加值等于峰压缩因子的倒数,这也与理论部分的结果一致.     

气体压缩因子和逸度因子的若干规律

在物理化学气体部分的教学内容中,气体的压缩因子和逸度因子均为重要概念,同时也是生产、科研和设计中的重要气体基础数据。本文通过对542种无机、有机气体的临界压缩因子数据进行整理及分析,对其数值取值范围及特点进行了讨论,同时对纯气体的压缩因子和逸度因子数值的一些简单规律进行了总结,为缺乏数据时二者的估算提供依据,以供教学参考。     

一个新的方阱流体状态方程

将方阱势能函数视为硬球势和一个短程均匀负势的叠加,并由统计力学方法导出了相应的状态方程,这个方程包含两个定标的径向分布函数.利用已知的压缩因子分子动力学模拟数据,回归得到了这两个径向分布函数,从而建立了一个新的方阱流体状态方程.它的吸引项要比Alder等人回归得到的简单得多,与方阱流体压缩因子的MD数据一致性也更好,特别是在高密度区域.     

谈压缩因子图的教学

压缩因子图主要用于对实际气体的计算,它是霍根-瓦特森(Hovgen-Watson)根据气体所遵循的共同函数关系即Z=f(Pr,Tr),对多种有机和无机气体进行测定,取其平均值绘制而成的.该图能在相当大的压力范围内得到比较满意的结果,所以在工业上有很大的实用价值,特别是对于高压气体的计算.与实际气体状态方程相比较,用压缩因子图计算气体的P、V、T性质不仅方便,而且所得的数据也较为准确.此外,还可以利用类似的图形来计算逸度、比热、焓等热力学函数.笔者认为压缩因子图是物理化学课程中不可忽视的一个组成部     

烷烃偏心因子和临界压缩因子的分子拓扑学研究

构建了一种新的拓扑指数ND,可对分子结构实现惟一性表征,具有优良的结构选择性.用ND指数对烷烃的偏心因子ω和临界压缩因子ZC进行研究,结果表明烷烃的偏心因子ω和临界压缩因子ZC可用下述二式来定量描述:ln(2.336 5ω)=0.008 288ND1 0.001 857ND2 0.000 551ND3 0.855 206;ln(ZC0.185)=0.021 496ND1 0.004 385ND2 0.001 235ND32.135 614,用上述二式分别对烷烃的偏心因子和临界压缩因子进行计算,计算值与实验值吻合良好.     

压缩X因子导数光谱法测定痕量锗

本采用压缩Ｘ因子导数光谱技术实现了宽峰体系灵敏度的大幅度提高，提出了测定痕量锗的方法。在０．７２ｍｏｌ／ＬＨ２ＳＯ４和３．０ｍｏｌ／ＬＨ３ＰＯ４的混酸介质中，锗－水杨基荧光酮－ＯＰ三元显色体系的压缩Ｘ因子四阶导数光谱摩尔响应系数达１．８９×１０＾６Ｌ．ｍｏｌ＾－１．ｃｍ＾－１，灵敏度比常规光度法高１２．４倍；最低检测出限为０．０００３３ｍｇ／Ｌ，比常规光谱法低４倍；选择性也进一步提高，绝大多数离     

压缩因子图与分子位能曲线的对应关系

根据对应状态定律,Hougen和Watson应用实验数据计算许多气体的压缩因子z,并将其平均值表示成对比参数(T_r,p_r)的函数,这样就建立了普遍化压缩因子图。只要稍加注意,不难发现,此图有一个显著的特点,各种不同的等T_r,曲线相交于两点:一点当p_r→0时,     

液相色谱梯度洗脱中的谱带压缩效应

谱带压缩效应是梯度洗脱区别于等度洗脱的重要特征。经典的范德姆特(van Deemter)理论塔板高度方程基于等度洗脱推导得到,因此不能对谱带压缩效应进行描述。在梯度洗脱中,保留因子(k)会随流动相组成(φ)的改变而发生变化,这就使得对梯度洗脱机理的研究要比等度洗脱复杂许多。该文对近10年来谱带压缩效应的研究进展,特别是溶剂强度模型(即描述ln k与φ关系的数学表达式)的非线性特征对谱带压缩因子(G)的影响进行了述评,指出为了更好地认识谱带压缩效应需要将这种非线性因素考虑在内。     

材料试验机测量位移功能扩展

介绍了自行设计的测量“弯曲－压缩”位移量的仪器与材料试验机的联要应用，该系统可测得精确的位移量，并可自动绘图，开发了原仪器设备的功能，提高了它的利用率和效率。     

不同品种环保橡胶填充油对乳聚丁苯橡胶性能影响研究

通过使用差示扫描量热仪(DSC)、橡胶加工分析仪(RPA)和动态压缩生热仪测试,分别研究了采用国内外不同品种的环保型橡胶填充油所制备的乳聚丁苯橡胶的热性能、动态力学性能以及动态压缩生热性能,并与非环保型丁苯橡胶SBR1712及环保型丁苯橡胶SBR1723进行了对比。结果表明,采用环保型芳烃油(TDAE)所制备的乳聚丁苯橡胶损耗因子最大,生热稍高于其它品种环保油;采用克拉玛依石化环保型环烷油(AP-10)所制备的乳聚丁苯橡胶动态压缩生热性能最好。     

Compressibility study of quaternary phospholipid blend monolayers

The mechanical properties of liposome membranes are strongly dependent on type and ratio of lipid compounds, which can have important role in drug targeting and release processes when liposome is used as drug carrier. In this work we have used Brewster's angle microscopy to monitor the lateral compression process of lipid monolayers containing as helper lipids either distearoyl phosphatidylethanolamine (DSPE) or dioleoyl phophatidylethanolamine (DOPE) molecules on the Langmuir trough. The compressibility coefficient was determined for lipid blend monolayers containing the helper lipids above, cholesterol, distearoyl phosphatidylcholine (DSPC) and pegylated-DSPE at room temperature. Two variables, the cholesterol fraction and the ratio ρ between the helper lipid (either DSPE or DOPE) and the reference lipid DSPC, were studied by multivariate analysis to evaluate their impact on the compressibility coefficient of the monolayers. The cholesterol level was found to be the most significant variable for DSPE blends while the ratio ρ was the most significant one for DOPE blend monolayers. It was also found that these two variables can exhibit positive interaction and the same compressibility value can be obtained with different blend compositions.     

Compressibility effects in packed and open tubular gas and supercritical fluid chromatography

The influence of the pressure drop on the efficiency and speed of analysis in packed and open tubular supercritical fluid chromatography (SFC) is described: methods previously developed to describe the effects of mobile phase compressibility on the performance of open tubular columns in SFC have been extended to packed columns. The Horvath and Lin equation has been used to elucidate the influence of variations in velocity, diffusivity, and capacity factor along the column on the overall efficiency of packed column SFC. In packed columns, in contrast with the situation in open tubular columns, because the increase in velocity is no longer compensated by an increase in diffusion coefficients, the increase in both linear velocity and capacity factor which result from a significant pressure drop cause the plate height to increase along the column. The effect of fluid decompression along the length of the column on the speed of analysis in SFC has been studied and numerical expressions derived which enable calculation of compressibility correction factors for the plate height. Both the f₁ and f₂ correction factors remain very close to unity for acceptable pressure drops, which means that the pressure drop has virtually no effect on the number of plates generated per unit time for an unretained component. For retained species, the decompression of the mobile phase across the column causes the capacity factor to increase and hence leads to increased analysis times.     

改进压缩性近似并导出新的硬球微扰理论表达式

提出在Barker与Henderson的压缩性近似推导中,相邻壳层之间的分子数应该相关,导出了相关系数和改进的二级微扰项,提高了高级微扰项在较高密度区的准确性。对二级以上的高级微扰项采用Barker与Henderson的近似方法,得到一个简单的微扰理论表达式,以硬球势为参考势,方阱势为微扰势,用一新的级数形式的径向分布函数导出了自由能、内能、比热、压缩因子的级数表达式。其四项截断式的计算结果与MC、MD计算机模拟值符合较好。     

Compressibility and thermal expansion coefficients of nanocomposites with amorphous and crystalline polymer matrix

Clay-containing polymeric nanocomposites (CPNC) with polystyrene (PS) or polyamide-6 (PA-6) matrix were studied within T = 300-600 K and P = 0.1-190 MPa. From the Pressure-Volume-Temperature (PVT) data the derivatives: compressibility, κ, and thermal expansion coefficient, α, were computed as functions of T, P and clay content, w. Dependence of these coefficients on P and T were significantly different for the amorphous PS than for the semi-crystalline PA-6. In the PS plots of κ and αvs.T the presence of secondary transitions, T_β/T_g ≈ 0.9 ± 0.1 and T_c/T_g = 1.2 ± 0.1, were detected and the clay effect at low T was prominent, affecting the physical aging. The isobaric values of α = α(T) were characterized by nearly T-independent values in the glassy and molten phase, connected by a large transitory region stretching from the ambient pressure values of T_g to T_c; this region was even more prominent in κ = κ(T). The derivative properties of PA-6 based CPNC were distinctly different. Here, the isobaric κ = κ(T) followed the same dependence on both sides of the melting zone, while the isobaric α = α(T) dependencies were dramatically different for the solid and molten phase; at T < T_mα linearly increased with T, after melting its value sharply decreased, and then at T > T_m (depending on w and P) either increased or decreased with T. Interpretation of the behavior in the melt and glass is based on the Simha-Somcynsky (S-S) cell-hole theory while that of the semicrystalline state on the Midha-Nanda-Simha-Jain (MNSJ) cell theory. In spite of the nonequilibrium conditions below the main transition point, T_g or T_m, the theories well predict the observed dependencies.     

An Equation for Viscosity and Isothermal Compressibility of Simple Liquids from a Closed-Form Expression for the Effective Viscosity of a Dispersed System

Abstract

Viscosity and isothermal compressibility of a simple liquid have been related by means of a closed-form equation for the low-shear viscosity of a liquid dispersion of solid particles. It involves macroscopic density, total correlation function and free volume. The equation achieved, which does not have an explicit solution, was approximated and applied to two sets of experimental data, where the free volume contribution was evaluated on the basis of experimental values of either volumes at zero fluidity or force constants for second virial coefficients and pair interaction potentials.     

Compressibility of CaZrO3 perovskite: Comparison with Ca-oxide perovskites

The evolution of the unit-cell parameters of CaZrO₃ perovskite, an orthorhombic perovskite belonging to space group Pbnm, have been determined to a pressure of 8.7 GPa at room temperature using single-crystal X-ray diffraction measurements. A fit of a third-order Birch-Murnaghan equation of state to the pressure-volume data yields values of V₀=258.04(2) Å³, K_T0=154(1) GPa and K₀′=5.9(3). Although CaZrO₃ perovskite does not exhibit any phase transitions in this pressure range, the compression of the structure is anisotropic with [010] approximately 20% less compressible than either [100] or [001]. Compressional moduli for the unit cell parameters are: K_a0=142(1) GPa and K_a0′=4.4(2), K_b0=177(2) GPa and K_b0′=9.4(5), K_c0=146(2) GPa and K_c0′=5.4(4). Comparison with other orthorhombic Ca-oxide perovskites shows that there is systematic increase in compressional anisotropy with increasing distortion from cubic symmetry.     

Compressibility of polymers

The compressibility of polyisobutylene and polystyrene above their glass transition temperature is treated as the sum of two parts; a free-volume compressibility and, as originally suggested by Bridgman, a compressibility of the molecules themselves. Two different models are used to treat the free-volume compressibility, and as a result values for the molecular compressibility are estimated. These are in reasonable agreement with other values in the literature. The magnitude of this “molecular compressibility” is then considered in relation to some existing treatments of intermolecular forces. These suggest that intermolecular contacts are more compressible than covalent bonds, and on this basis the observed levels of molecular compressibility can be explained.     

Compressibility of Gas Hydrates

Experimental data on the pressure dependence of unit cell parameters for the gas hydrates of ethane (cubic structure I, pressure range 0–2 GPa), xenon (cubic structure I, pressure range 0–1.5 GPa) and the double hydrate of tetrahydrofuran+xenon (cubic structure II, pressure range 0–3 GPa) are presented. Approximation of the data using the cubic Birch–Murnaghan equation, P=1.5B₀[(V₀/V)^7/3?(V₀/V)^5/3], gave the following results: for ethane hydrate V₀=1781 ų, B₀=11.2 GPa; for xenon hydrate V₀=1726 ų, B₀=9.3 GPa; for the double hydrate of tetrahydrofuran+xenon V₀=5323 ų, B₀=8.8 GPa. In the last case, the approximation was performed within the pressure range 0–1.5 GPa; it is impossible to describe the results within a broader pressure range using the cubic Birch–Murnaghan equation. At the maximum pressure of the existence of the double hydrate of tetrahydrofuran+xenon (3.1 GPa), the unit cell volume was 86 % of the unit cell volume at zero pressure. Analysis of the experimental data obtained by us and data available from the literature showed that 1) the bulk modulus of gas hydrates with classical polyhedral structures, in most cases, are close to each other and 2) the bulk modulus is mainly determined by the elasticity of the hydrogen‐bonded water framework. Variable filling of the cavities with guest molecules also has a substantial effect on the bulk modulus. On the basis of the obtained results, we concluded that the bulk modulus of gas hydrates with classical polyhedral structures and existing at pressures up to 1.5 GPa was equal to (9±2) GPa. In cases when data on the equations of state for the hydrates were unavailable, the indicated values may be recommended as the most probable ones.     

Rapidly Estimating Natural Gas Compressibility Factor

Natural gases containing sour components exhibit different gas compressibility factor(Z) behavior than do sweet gases.Therefore,a new accurate method should be developed to account for these differences.Several methods are available today for calculating the Z-factor from an cquation of state. However,these equations are more complex than the foregoing correlations,involving a large number of parameters,which require more complicated and longer computations.The aim of this study is to develop a simplified calculation method for a rapid estimating Z-factor for sour natural gases containing as much as 90% total acid gas.In this article,two new correlations are first presented for calculating the pseudo- critical pressure and temperature of the gas mixture as a function of the gas specific gravity.Then,a simple correlation on the basis of the standard gas compressibility factor chart is introduced for a quick estimation of sweet gases' compressibility factor as a function of reduced pressure and temperature.Finally,a new corrective term related to the mole fractions of carbon dioxide and hydrogen sulfide is developed.