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Transport, thermodynamics processes

Figure 10. Equilibria between ligand and receptor in the homogeneous phase and at the heterogeneous phase. Non-blocked receptors diffuse by a transport-limited process to the surface and can form a second equilibrium. From this assay type, kinetic as well as thermodynamic constants can be determined. Figure 10. Equilibria between ligand and receptor in the homogeneous phase and at the heterogeneous phase. Non-blocked receptors diffuse by a transport-limited process to the surface and can form a second equilibrium. From this assay type, kinetic as well as thermodynamic constants can be determined.
Chapter 8 presents problems of natural gas production, transportation, and processing which are related to hydrates. Because a standard kinetic treatment method has progressed past the fledgling state in the second edition (1998), the state-of-the-art in flow assurance is turning away from thermodynamic properties which encourage hydrate avoidance, to kinetic properties which encourage a new philosophy in flow assurance—that of risk management. [Pg.314]

A model for transient simulation of radial and axial composition and temperature profiles In pressurized dry ash and slagging moving bed gasifiers Is described. The model Is based on mass and energy balances, thermodynamics, and kinetic and transport rate processes. Particle and gas temperatures are taken to be equal. Computation Is done using orthogonal collocation In the radial variable and exponential collocation In time, with numerical Integration In the axial direction. [Pg.359]

This quantity has a key significance for electrochemistry and irreversible -> thermodynamics, and it is used for the description of most transport-related processes and chemical reactions [ii-iv]. For -> equilibrium under zero electrical and magnetic fields... [Pg.91]

Hydrogeochemical models are dependent on the quality of the chemical analyses, the boundary conditions presumed by the program, theoretical concepts (e.g. calculation of activity coefficients) and the thermodynamic data. Therefore it is vital to check the results critically. For that, a basic knowledge about chemical and thermodynamic processes is required and will be outlined briefly in the following chapters on hydrogeochemical equilibrium (chapter 1.1), kinetics (chapter 1.2), and transport (chapter 1.3). Chapter 2 gives an overview on standard... [Pg.204]

Active transport a process in which solute molecules or ions move across a biomembrane against a concentration gradient. Since thermodynamic work... [Pg.10]

The purpose of this chapter is to underline the importance of transport phenomena and mathematical modelling in biomedical applications where a thermodynamic system, not in an equilibrium condition, undergoes a spontaneous irreversible transformation, as in classic drug delivery systems. The irreversibility of thermodynamic processes was thoroughly investigated from a mathematical point of view, using phenomenological and kinetic approaches. Three biomedical examples were analysed in detail membranes... [Pg.94]

This crucial step in the design of the chemical plant involves all subareas of chemical engineering reaction engineering, thermodynamics, process control, unit operations and transport, and material and energy balances. Each is applied to put details into the six general sections of the GBFD—reactor feed preparation, reactor, separator feed preparation, separator, recycle, and environmental control. [Pg.377]

The tme driving force for any diffusive transport process is the gradient of chemical potential rather than the gradient of concentration. This distinction is not important in dilute systems where thermodynamically ideal behavior is approached. However, it becomes important at higher concentration levels and in micropore and surface diffusion. To a first approximation the expression for the diffusive flux may be written... [Pg.258]

Electron Transport Between Photosystem I and Photosystem II Inhibitors. The interaction between PSI and PSII reaction centers (Fig. 1) depends on the thermodynamically favored transfer of electrons from low redox potential carriers to carriers of higher redox potential. This process serves to communicate reducing equivalents between the two photosystem complexes. Photosynthetic and respiratory membranes of both eukaryotes and prokaryotes contain stmctures that serve to oxidize low potential quinols while reducing high potential metaHoproteins (40). In plant thylakoid membranes, this complex is usually referred to as the cytochrome b /f complex, or plastoquinolplastocyanin oxidoreductase, which oxidizes plastoquinol reduced in PSII and reduces plastocyanin oxidized in PSI (25,41). Some diphenyl ethers, eg, 2,4-dinitrophenyl 2 -iodo-3 -methyl-4 -nitro-6 -isopropylphenyl ether [69311-70-2] (DNP-INT), and the quinone analogues,... [Pg.40]

The scientific basis of extractive metallurgy is inorganic physical chemistry, mainly chemical thermodynamics and kinetics (see Thermodynamic properties). Metallurgical engineering reties on basic chemical engineering science, material and energy balances, and heat and mass transport. Metallurgical systems, however, are often complex. Scale-up from the bench to the commercial plant is more difficult than for other chemical processes. [Pg.162]

R. A. Home, ed.. Water andMqueous Solutions Structure, Thermodynamics, and Transport Processes, Wiley-Interscience, New York, 1972. [Pg.218]

These reactions are thermodynamically unfavorable at temperatures below ca 1500°C. However, at temperatures in the range from 1000 to 1200°C a small but finite equiUbrium pressure of barium vapor is formed at the reaction site. By means of a vacuum pump, the barium vapor can be transported to a cooled region of the reactor where condensation takes place. This destroys the equiUbrium at the reaction site and allows more barium vapor to be formed. The process is completely analogous to that used in the thermal reduction of CaO with aluminum to produce metallic calcium (see Calcium AND CALCIUM alloys). [Pg.472]

The use of the computer in the design of chemical processes requires a framework for depiction and computation completely different from that of traditional CAD/CAM appHcations. Eor this reason, most practitioners use computer-aided process design to designate those approaches that are used to model the performance of individual unit operations, to compute heat and material balances, and to perform thermodynamic and transport analyses. Typical process simulators have, at their core, techniques for the management of massive arrays of data, computational engines to solve sparse matrices, and unit-operation-specific computational subroutines. [Pg.64]

The industrial economy depends heavily on electrochemical processes. Electrochemical systems have inherent advantages such as ambient temperature operation, easily controlled reaction rates, and minimal environmental impact (qv). Electrosynthesis is used in a number of commercial processes. Batteries and fuel cells, used for the interconversion and storage of energy, are not limited by the Carnot efficiency of thermal devices. Corrosion, another electrochemical process, is estimated to cost hundreds of millions of dollars aimuaUy in the United States alone (see Corrosion and CORROSION control). Electrochemical systems can be described using the fundamental principles of thermodynamics, kinetics, and transport phenomena. [Pg.62]

The third term on the right side of equation 11 is the corresponding ratio of the mean molar activity coefficients. The fourth and last term results from transport processes in the junction region, and carmot be determined from thermodynamics. This term is often small and is not treated here. Neglecting this junction region and activity corrections leads to... [Pg.63]

Predicting the cell potential requires knowledge of thermodynamic properties and transport processes ia the cell. Conversely, the measurement of cell potentials can be used to determine both thermodynamic and transport properties (4). [Pg.63]


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