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A. D. Pelton  P. L. Lin 《Calphad》1983,7(4):295-303
Phase diagrams of the quaternary reciprocal salt systems Li, Na, K/CO3, SO4; Li, Na/CO3, SO4, OH; Li, K/CO3, SO4, OH; and Na, K/CO3, SO4, OH (the last three up to 10 mol % hydroxide) were calculated from the optimised thermodynamic properties of their sub-systems via the Conformal Ionic Solution Theory by means of a computer program designed for the purpose.  相似文献   

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为解决标准设计模式演化后难以检测的问题,引入设计模式变体思想,以Bridge模式为例,给出了八种常用的变体实现,并以人工形式挖掘了四种开源系统中Bridge模式变体的基准数,接着在Apache Ant1.6.2与JHotDraw5.1开源系统中通过六种主流设计模式检测工具进行了变体检测实验。试验结果表明,FCA-CBR方法简单有效,对2种开源系统中Bridge模式变体检测的精确率达到60%与48.1%,与先前方法相比有了较大的提高。  相似文献   

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In order to develop the nitrate deposits found close to Lop Nur in the Xinjiang region in China, the solubilities of the system Na+,Mg2+/Cl,SO42−, NO3–H2O and its subsystems, the quaternary systems Na+,Mg2+/SO42−,NO3–H2O and Mg2+/Cl,SO42−,NO3–H2O, were studied at 298.15 K. The phase diagrams were plotted according to the solubilities achieved. In the equilibrium phase diagram of Mg2+/Cl,SO42−,NO3–H2O, there are two invariant points, five univariant curves and four regions of crystallization: Mg(NO3)26H2O,MgCl26H2O,MgSO47H2O and MgSO4(1–6)H2O. In the equilibrium phase diagram of Na+,Mg2+/SO42−, NO3–H2O, there are five invariant points, eleven univariant curves and seven regions of crystallization: Na2SO4,Na2SO410H2O,NaNO3,MgSO4Na2SO44H2O,NaNO3Na2SO42H2O,Mg(NO3)26H2O and MgSO47H2O. In the equilibrium phase diagram of the Na+, Mg2+/Cl,SO42−,NO3–H2O system, there are six invariant points, and ten regions of crystallization: NaCl, NaNO3,Na2SO4,Na2SO410H2O,MgSO4Na2SO44H2O, NaNO3Na2SO42H2O,MgCl26H2O,Mg(NO3)26H2O, MgSO4(1–6)H2O and MgSO47H2O.  相似文献   

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The liquidus in the high basicity region in the Al2O3(30 mass%)-CaO-MgO-SiO2 system were determined experimentally at 1773 and 1873 K using the quench technique followed by EPMA analysis. Based on the experimental data, a phase diagram of the Al2O3(30 mass%)-CaO-MgO-SiO2(<20 mass%) section was constructed for 1773 and 1873 K. The solubilities of 2CaO.SiO2 and 3CaO.SiO2 at 1773 K were found to be considerably higher in comparison with the existing phase diagram. Even the solubility of MgO at 1873 K was found to be somewhat higher. In addition, the activities of MgO, CaO and Al2O3 at 1773 K were estimated using the phase diagram information.  相似文献   

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In this paper we will consider systems with linear time-invariant perturbations. We will analyze robust performance in the ?2 and ? settings. The ?2 setting gives rise to the familiar case of structured singular values, and a stability criterion is given by the “small μ” theorem. We show that although the necessary and sufficient criterion of robust stability for the ? case (? stability with structured ?-gain bounded perturbations) is the same “small μ” criterion, a system with ?2-gain bounded perturbations is never ? stable.  相似文献   

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Available phase diagram and thermodynamic data on the eighteen binary systems containing Li+ , Na+, K+, S04=, CO3=, and OH have been collected and critically assessed. A set of self-consistent thermodynamic parameters describing the free energies of the compounds, solid solutions, and liquid solutions in the binary systems has been formulated. The phase diagrams have been calculated, and estimated error limits of all diagrams are given.  相似文献   

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针对目前卫星复杂化、多任务、集群化发展大趋势,利用传统的性能穷举法及单性能评估法进行卫星的综合效能评估已经无法满足,对卫星综合效能指标体系进行研究,以微纳集群卫星为例,分层列举了相关指标体系,对卫星综合效能评估方法进行了研究,介绍了一般效能评估流程,提出了一种改进的模糊推理效能评估方法,该方法在原有单因素评估指标模糊推理的基础上,加入了指标间的多因素比较,并与层次分析相结合。最后以实际导航卫星为例进行仿真分析,分析结果表明该方法切实可行,效能评估结果正确有效,为复杂卫星系统提高其综合效能提供保障。  相似文献   

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For a linear time-invariant system with several disturbance inputs and controlled outputs, we show how to minimize the nominal H2-norm performance in one channel while keeping bounds on the H2-norm or H-norm performance (implying robust stability) in the other channels. This multiobjective H2 /H-problem in an infinite dimensional space is reduced to sequences of finite dimensional convex optimization problems. We show how to compute the optimal value and how to numerically detect the existence of a rational optimal controller. If it exists, we reveal how the novel trick of optimizing the trace norm of the Youla parameter over certain convex constraints allows one to design a nearly optimal controller whose Youla parameter is of the same order as the optimal one  相似文献   

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High-purity distillation columns are known to be difficult to control due to their ill-conditioned and non-linear behaviour. Two approaches for the design of robust controllers yielding high performance are presented. For the first approach, first principles are used to develop an uncertainty model describing the nonlinear dynamics within the entire operating range of an industrial distillation column. This structured uncertainty model is used for μ-synthesis. In a second approach which is based on loop shaping ideas, an H-controller is designed. This controller performs as well as the μ-controller. The H-approach offers the advantage that the burden for uncertainty modelling and computation is greatly reduced. However, the GS/T augmentation scheme, which is developed in this paper, must be used for the design of the H-controller to avoid the inversion of the plant in the controller. The paper concludes with a comparison of the H- and μ-synthesis methods.  相似文献   

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