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991.
Hyun Jung Kim 《Thermochimica Acta》2006,441(2):168-175
The eutectic melting of a CBZ-l-Asp/l-PheOMe·HCl model mixture was investigated in kinetic, thermal, thermodynamic, rheological, and morphological aspects. From TX-phase diagrams, the eutectic composition was determined to be 0.55 M fraction of CBZ-l-Asp. The highest melting rate and the lowest apparent viscosity in the range of 55-75 °C were obtained at the eutectic composition. Using Arrhenius plots of melting rates and apparent viscosities, minimum activation energies in the range of 60-80 °C were obtained at the eutectic composition, whereas maximum values were attained below 60 °C. At the eutectic composition, the maximum heat of fusion, the lowest excess free energy, and the highest excess entropy values were observed by differential scanning calorimetry (DSC). A highly homogeneous morphology due to rearrangement of molecules was observed in the eutectic mixture via scanning electron microscopy and X-ray diffraction analysis. IR spectra revealed that hydrogen bonding in the mixture increases during eutectic melting. 相似文献
992.
993.
In the spirit of the classical random central limit theorem a general limit theorem for random stopping in the scheme of infinitesimal triangular arrays on a separable metrizable group is presented. The approach incorporates and generalizes earlier results for normalized sequences of independent random variables on both separable Banach spaces and simply connected nilpotent Lie groups originated by Siegel and Hazod, respectively. (© 2007 WILEY‐VCH Verlag GmbH & Co. KGaA, Weinheim) 相似文献
994.
为了解决传统水下目标跟踪中目标数目估计不准确、状态估计误差增长过快的问题,提出了一种基于高斯混合概率假设滤波的水下目标跟踪算法。该算法基于双基地观测模型,采用高斯混合概率假设滤波算法处理方位和时延信息,利用粒子群算法处理多普勒频率获得矢量速度,进一步提升算法的跟踪精度。结果表明,该算法能完成在杂波环境下对目标的跟踪,相比传统的关联算法,能够有效地实现目标个数估计和抑制状态误差增长的目的。 相似文献
995.
Having a valid mathematical model for structureless emission band shapes is important when deconvoluting fluorescence spectra
of complex molecules. We propose a new asymmetric model for emission spectra of five organic molecules containing aromatic
ring: catechol, coniferyl alcohol, hydroquinone, phenylalanine and tryptophan. For each molecule, a series of emission spectra,
varying in excitation wavelength, were fitted with the new model as well as with two other analytical expressions: log-normal,
described previously in the literature, and sigmoid-exponential. Their deconvolution into two, three and four Gaussian components
was also performed, in order to estimate the number of symmetric components needed to obtain a better fitting quality than
that of the asymmetric models. Four subtypes of the new model, as well as the log-normal one, did not differ significantly
in their fitting errors, while the sigmoid-exponential model showed a significantly worse fit. Spectra of two mixtures: hydroquinone–coniferyl
alcohol and hydroquinone–tryptophan were deconvoluted into two asymmetric and four Gaussian components. Positions of asymmetric
components of mixtures matched those of separate molecules, while Gaussian did not. Component analysis of a polymer molecule,
lignin, was also performed. In this more complex case asymmetric and Gaussian components also grouped in alternating positions. 相似文献
996.
The influence of different solvents on the extraction medium and the RP-HPLC mobile phase composition were investigated by statistical mixture designs to optimize solvent proportions to prepare the fingerprint of a medicinal herbal extract. For modeling, the number of peaks was used as a measure of fingerprint information. The optimum compositions of solvent to extract chemical substances from green tea and for mobile phase chromatographic analysis were ethyl acetate/ ethanol/dichloromethane (20:5:75 v/v/v) and MeOH/ACN/water (7.5:57.5:35 v/v/v), respectively. This system results in 26 peaks in the chromatographic fingerprint. These results show that an incorrect choice of modifiers for mobile phase composition and solvent extraction hampers the detection of a maximum number of peaks and produces a poor chromatographic fingerprint. 相似文献
997.
Amathematical model to simulate the dilute-acid hydrolysis process of cellulose particles is presented. In this model, the
mass is treated as a mixture of different components. A test case is considered for which transport equations for components
are developed and solved together with the momentum equation for the fluid flow. To solve the model equations, a commercially
available flow solver was used. All input data were taken from previously published works. For the small static mixer considered
as test geometry, the result, in terms of the conversion of the cellulose particles, was reasonable. With input parameters
that are relevant to a plant-size reactor, the model can be used to predict the conversion of both cellulose and hemicellulose
particles. 相似文献
998.
The number of droplets which may be formed with a supersaturated vapor in presence of a gas cannot exceed a number proportional to (pv−pv0)4 where pv and pv0 denote at the same temperature the pressure of the supersaturated vapor–gas mixture and the pressure of the saturated vapor–gas mixture. The energy necessary to the droplet formation is also bounded by a number proportional to (pv−pv0)2. 相似文献
999.
Local heat transfer and pressure drop measurements were made during condensation of a zeotropic CFC114-CFCll3 refrigerant mixture in the annulus of a double-tube coil consisting of three U-bends and four straight lengths. The inner tube is a 19.1-mm O.D. corrugated copper tube with wire fins soldered onto the outer surface and the inner diameter of the outer duct is 25.0 mm. The vapor-phase mass transfer coefficient exhibited a sawtooth behavior with the U-bends showing higher coefficients than the straight lengths. The frictional pressure gradient data agreed well with a previously developed empirical equation for the condensation of pure refrigerants. A prediction method for the condensation heat transfer rate was proposed on the basis of the correlations of the vapor-phase mass transfer coefficient and heat transfer coefficient of the condensate film. The heat transfer data were correlated by the present method to a mean absolute deviation of 12.9%. 相似文献
1000.
Summary Samples of stable coal-oil mixtures were prepared with coal concentrations ranging from 30–50% by weight. Extensive rheological data were obtained using capillary and cone-plate viscometers for samples of coal-oil mixtures and fuel-oil which served as a reference fluid. Viscosity measurements show coal-oil mixtures to be shear-thinning suspensions, i.e., the viscosity decreases moderately with increasing shear rates. In the concentration range of 30–40% coal, the coal-oil mixture shows a predominantly Newtonian behavior. For mixtures with coal concentrations higher than 40%, a yield point was observed. The study of these samples with the rotating-rod viscometer indicated a migration of coal particles away from the rotating rod with no noticeable rod climbing, thus no evidence of normal stress effects. The rheological data can be represented by any of the three two-parameter models: Power Law, Bingham Plastic, or Casson, with the last two models being more realistic and consistent with the observations.With 9 figures 相似文献