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排序方式: 共有965条查询结果,搜索用时 46 毫秒
1.
现有毒品滥用流行病模型假设吸毒者康复后对毒品拥有永久"免疫"力,而忽视了其再次成为毒品易感者的可能性。针对这一问题,通过考虑社区治疗和隔离治疗两种措施,分析了毒品滥用人群的演化过程,提出了基于暂时"免疫"力的毒品滥用流行病模型,并计算了模型的基本再生数,讨论了模型平衡点的存在性和稳定性。当基本再生数小于1时,模型存在一个局部渐进稳定的无毒平衡点;当基本再生数大于1时,模型存在唯一的地方病平衡点,并利用几何方法证明了地方病平衡点的全局稳定性;当基本再生数等于1时,如果满足一定条件,模型出现后向分支现象。数值模拟验证了上述所有结果。研究结果表明提高隔离治疗率、改善社区治疗效果和降低接触传染率可以有效抑制毒品滥用的流行。 相似文献
2.
Shuichi Yamamoto Teruaki Morihiro Koichi Ariyoshi Turkan Aktas 《Drying Technology》2005,23(6):1319-1330
As the surface properties of the drying materials are very important not only for the drying rate but also for the quality change during drying, the effects of surface concentration on the drying behavior of liquid foods (sugar solutions) were investigated by isothermal drying experiments and by numerical calculation experiments. The isothermal drying experiments with gelled sugar solution systems (sucrose and maltodextrin) were carried out at various relative humidity (RH) values (RH = 0 to 84%). Separate experiments were carried out for determination of the desorption isotherms.
The isothermal drying curves of sugar solutions at RH = 0 to 51% were very similar. Numerical simulations also showed that the drying curves of these sugars at the surface concentration = 0 and 0.1 are almost the same, although the concentration distributions are different.
When a small amount of gelatin was added to sugar solutions, the drying rate decreased remarkably as the gelatin might form a thin film (skin) near the surface, and consequently the retention of ethanol increased. 相似文献
The isothermal drying curves of sugar solutions at RH = 0 to 51% were very similar. Numerical simulations also showed that the drying curves of these sugars at the surface concentration = 0 and 0.1 are almost the same, although the concentration distributions are different.
When a small amount of gelatin was added to sugar solutions, the drying rate decreased remarkably as the gelatin might form a thin film (skin) near the surface, and consequently the retention of ethanol increased. 相似文献
3.
连续双向联想记忆模型的稳定性分析 总被引:6,自引:0,他引:6
对于连续型Hopfield模型的平衡态特征,目前人们已经得到了很多富有意义的成果,本文说明,连续Hopfield模型的大部分结论都可以推广到连续双向联想记忆模型,我们重点讨论了平衡态条件、渐近稳定性以及围绕一稳定平衡点的吸引域等问题,所得到的结论对于BAM的设计和应用都是很有意义的。 相似文献
4.
The distribution ratios of Fe and B between molten Fe–B alloy and molten Ag were measured at temperatures between 1573 and 1923 K. Also, distribution ratios of Fe and B between molten Fe–B–Csatd. alloys and molten Ag were measured at 1873 K. It was found that the excess Gibbs free energy of mixing in molten Fe–B and Fe–B–C alloys can be expressed by utilizing the Redlich–Kister polynomial. The activity curves of the elements in molten Fe–B alloy and Fe–B–C alloy were estimated. 相似文献
5.
会计信息失真现象的博弈分析 总被引:2,自引:0,他引:2
在对现实进行合理假定的基础上建立了会计信息失真现象的有限完美信息动态博弈模型,并利用后退归纳法找到了五个满足不同条件的纳什均衡解。通过对均衡条件的分析,找出了导致会计信息失真的治理结构原因和法律制度因素,并提出了建设性的解决措施。 相似文献
6.
E.I.P. Volcke M. Loccufier P.A. Vanrolleghem E.J.L. Noldus 《Journal of Process Control》2006,16(10):1003-1012
This paper addresses the dynamics of a SHARON reactor, a promising technology for ammonium removal from concentrated wastewater streams. The contraction mapping theorem is used to determine which operating conditions of a SHARON reactor with pH-control result in a unique equilibrium state. However, this approach only identifies the case of very large dilution rates, in practice corresponding with complete biomass wash-out, i.e. with complete loss of biological activity. Practical operation of a SHARON reactor aims at reaching ammonium conversion to nitrite. To identify such interesting operating points, the equilibrium points are subsequently calculated directly in terms of input variables for a simplified SHARON reactor model. The stability of the obtained equilibrium points is assessed and the corresponding phase portraits are analyzed. The influence of slightly varying parameter and input values is investigated as well. 相似文献
7.
W. Jill Harrison K. R. Pearson Alan A. Powell E. John Small 《Computational Economics》1994,7(3):203-223
General equilibrium moels are usually represented as a system of levels equations (e.g., in North America) or a system of linearized equations (e.g., in Australia). Either representation can be used to obtain accurate solutions. General-purpose software is available in both cases-GAMS or MPS/GE is typically used by levels modellers and GEMPACK by linearizers. Some equations (notably accounting identities) are naturally expressed in the levels while others (especially behavioural equations) are naturally expressed in a linearized form. This paper describes the new GEMPACK facility for solving models represented as a mixture of levels and linearized equations and discusses the advantages to modellers of using such a representation. 相似文献
8.
Krzysztof Kaczmarski Dongmei Zhou Georges Guiochon 《Chemical engineering science》2003,58(11):2325-2338
The adsorption isotherm data of R- and S-1-indanol and of their racemic mixture on cellulose tribenzoate were measured by frontal analysis. These experimental data were fitted to the single-component and the modified competitive Bilangmuir isotherms. The overloaded elution profiles of bands of the pure enantiomers and of the racemic mixture were calculated for different sample sizes, using the best competitive isotherm model and the General Rate Model of chromatography coupled with the generalized Maxwell-Stefan equation that describes the surface diffusion flux. The calculated and the experimental profiles were found to be in excellent agreement in all cases. The parameters of the model of the mass transfer kinetics were derived from the band profiles obtained for the pure enantiomers. The same values of these parameters give an excellent prediction of the profiles of multicomponent bands. The new model described here allows a satisfactory interpretation of the competitive mass transfer kinetics. 相似文献
9.
The liquid-liquid equilibrium for the quaternary system of o-xylene(1)+water(2)+propionic acid(3)+1-butanol(4) was measured
at 298.15 K and atmospheric pressure. Binodal curves, tie-lines, a distribution curve, and a selectivity curve for the quaternary
system have been determined in order to investigate the effect of binary solvents, oxylene and 1-butanol, on extracting propionic
acid from aqueous solution. In addition, these experimental tie line data were also compared with the values predicted by
the UNIFAC model. In this study, the UNIFAC model was capable of predicting the compositions of this quaternary system within
an average RMSD of 1.13 mol%.
This paper was prepared at the 2004 Korea/Japan/Taiwan Chemical Engineering Conference held at Busan, Korea between November
3 and 4, 2004. 相似文献
10.
An algorithm has been developed and tested for steady-state liquid-liquid extraction, using rectangular coordinates. It is capable of handling common types of stagewise contact, i.e., single stage extraction, multistage cross-current, and continuous countercurrent multistage extraction. The results depend on the nature of the extraction scheme and the extent of separation desired. While equilibrium data for some systems are stored in its data bank, the present portable computer simulator ( LIQEXT) has the flexibility of reading equilibrium data for other systems, as well as overriding stored data
Both design and rating cases can be performed. In the design mode, i.e., given the feed and solvent rates and the outlet concentration, it calculates the number of stages, the exit stream flow rates, and the concentration profile. In the rating ( or simulation) mode, i.e., given the feed and solvent rates, and the number of stages, it computes the exit streams flow rates and compositions, and the concentration profile. In both cases a graphical output of the concentration profile is produced, either on the screen or on a hard-copy plotter. 相似文献
Both design and rating cases can be performed. In the design mode, i.e., given the feed and solvent rates and the outlet concentration, it calculates the number of stages, the exit stream flow rates, and the concentration profile. In the rating ( or simulation) mode, i.e., given the feed and solvent rates, and the number of stages, it computes the exit streams flow rates and compositions, and the concentration profile. In both cases a graphical output of the concentration profile is produced, either on the screen or on a hard-copy plotter. 相似文献