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Characterization of the Process

2 Self-Propagating High-Temperature Synthesis of Hard Materials [Pg.328]

As indicated above, determination of the kinetic parameters of the SHS process can be made through a mathematical analysis of temperature profiles [14]. Integration of an adiabatic form of Eq. (1) along with appropriate substitutions gives the following expression for the conversion parameter [9], [Pg.328]

Similar analyses were made for the synthesis of MoSi2 and Ti2Si3 [11]. In these cases, particularly for MoSi2, the reaction is not complete within a narrow zone as can be seen from Fig. 11. Here the width of the zone is calculated as approximately 1.3 mm. The wide reaction zone for molybdenum silicide is, in part, the consequence of a relatively low enthalpy of formation as manifested by an adiabatic temperature near the empirically established lower limit. This is the reason why some composites of MoSi2 cannot be directly synthesized by SHS without some form of activation. [Pg.330]


The overall set of partial differential equations that can be considered as a mathematical characterization of the processing system of gas-liquid dispersions should include such environmental parameters as composition, temperature, and velocity, in addition to the equations of bubble-size and residence-time distributions that describe the dependence of bubble nucleation and growth on the bubble environmental factors. A simultaneous solution of this set of differential equations with the appropriate initial and boundary conditions is needed to evaluate the behavior of the system. Subject to the Curie principle, this set of equations should include the possibilities of coupling effects among the various fluxes involved. In dispersions, the possibilities of couplings between fluxes that differ from each other by an odd tensorial rank exist. (An example is the coupling effect between diffusion of surfactants and the hydrodynamics of bubble velocity as treated in Section III.) As yet no analytical solution of the complete set of equations has been found because of the mathematical difficulties involved. To simplify matters, the pertinent transfer equation is usually solved independently, with some simplifying assumptions. [Pg.333]

Liquid membrane type ion-seleetive electrodes (ISEs) provide one of the most versatile sensing methods because it is possible to customize the sensory elements to suit the structure of the analyte. A wealth of different synthetic and natural ionophores has been developed, in the past 30 years, for use in liquid membrane type ISEs for various inorganic and organic ions [1], In extensive studies [2-4], the response mechanism of these ISEs has been interpreted in terms of thermodynamics and kinetics. However, there have been few achievements in the characterization of the processes occurring at the surface of ISEs at molecular level. [Pg.442]

In order to gain an insight into the mechanism on the basis of the slope of a Type A correlation requires a more complicated procedure. Consider the Hammett equation. The usual statement that electrophilic reactions exhibit negative slopes and nucleophilic ones positive slopes may not be true, especially when the values of the slopes are low. The correct interpretation has to take the reference process into account, for example, the dissociation equilibrium of substituted benzoic acids at 25°C in water for which the slope was taken, by definition, as unity (p = 1). The precise characterization of the process under study is therefore that it is more or less nucleophilic than the reference process. However, one also must consider the possible influence of temperature on the value of the slope when the catalytic reaction has been studied under elevated temperatures there is disagreement in the literature over the extent of this influence (cf. 20,39). The sign and value of the slope also depend on the solvent. The situation is similar or a little more complex with the Taft equation, in which the separation of the molecule into the substituent, link, and reaction center may be arbitrary and may strongly influence the values of the slopes obtained. This problem has been discussed by Criado (33) with respect to catalytic reactions. [Pg.161]

The identification and characterization of the processes of GPCR activation and inactivation have defined the genomics of the accessory proteins necessary to these processes. This has accelerated progress in understanding the fundamental mechanisms involved in GPCR synthesis, transport to the membrane, ligand binding, and activation and inactivation by GRK-mediated (and other) phosphorylation (192). [Pg.97]

Before discussing the various reactions in more detail in the following sections, a short characterization of the processes and a description of the types of catalyst involved will be given. [Pg.135]

Challenging of Critical Process Parameters or Characterization of the Process... [Pg.55]

This characterization of the process of tablet formation has to be completed by analyzing the changes induced by tableting. [Pg.1082]

The applications of LSV and CV to the study of chemical processes following an electron transfer reaction are so numerous that a review of the subject is clearly beyond the scope of this chapter. The examples were selected to demonstrate the application of the techniques in practical work. Although obvious, it should be emphasized that electrochemical reactions are not different from any other chemical reaction and, therefore, that the whole arsenal of methods of attack known from conventional kinetics may be used in the characterization of the process. This includes also temperature [85,120,136-138] and kinetic isotope effects [138,139]. [Pg.128]

Benson, J. M. Hill, J. 0. Royer, R. E. Hanson, R. L. Mitchell, C. E. Newton, G. J., "Toxicological Characterization of the Process Stream and Effluents of a Low Btu Coal Gasifer," in Proceedings of the 20th Hanford Life Sciences Symposium, Richland, Washington, 1980, in press. [Pg.224]

Komfeld, S. and Komfeld, R. (1971) The Structure of the Phytohaemagglutinin Receptor Sites from Human Erythrocytes , Journal of Biological Chemistry, 245 2536-45 Komfeld, S., Li, E. Tabas, I. (1978) The Synthesis of Complex-type Oligosaccharides II Characterization of the Processing Intermediates in the Synthesis of the Complex Oligosaccharide Units of Vesicular Stomatitis Vims G Protein , Journal of Biological Chemistry, 253, 7771-8... [Pg.328]

To demonstrate the proposed techniques, two case studies are presented that foDow the procedure from characterization of the processes through to performance assessment of a pertinent set of controllers. [Pg.59]

The anode/electrolyte interphase (the SEI) plays a key role in lithium-metal, lithium-alloy and lithium-ion batteries. Today we have some understanding of the first lithium intercalation step into carbon and of the processes taking place on the lithium-metal anode. A combination of a variety of analytical tools including dilatometry, STM, AFM, XPS, EDS, SEM, XRD, QCMB, FTIR, NMR, EPR, TOP SIMS, Raman spectroscopy, AC impedance measurements and DSC is used in order to gain a comprehensive characterization of the processes occurring at the anode/electrolyte interphase. An understanding of SEI-related phenomena is crucial for the development of safer and better lithium-based batteries. [Pg.59]

It has been shown that the results from the electrochemically investigation during the fuel cell procedure and the post-mortem and also ex situ p-CT analysis coincide and the combination of both investigation allow a comprehensive characterization of the processes within an HT-PEM MEA. [Pg.378]

Schlogl s article shows why. He tells of the application of old and new techniques to the characterization of the processes, phases, and interfaces occurring in the evolution of the working catalyst from its oxide precursors. He arrives at conclusions which are quite similar to those derived from chemical principles, while finding further complexities. It is in this area that surface physics demonstrates its greatest value to applied catalysts. [Pg.461]

The results, described in the previous sections, are used to create a dimensionless description of the superheated atomization. The characterization of the process has to start with the flow behavior through the nozzle, since aU spray characteristics are a result of the phenomena taking place inside the atomizer. [Pg.636]

Eor the characterization of the process behavior within the drop column and depending on the surfactants used, the method of a particle-free phase transfer was applied. [Pg.387]


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