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Isothermal state

Temperature influences skin permeability in both physical and physiological ways. For instance, activation energies for diffusion of small nonelectrolytes across the stratum corneum have been shown to lie between 8 and 15 kcal/mole [4,32]. Thus thermal activation alone can double the rate skin permeability when there is a 10°C change in the surface temperature of the skin [33], Additionally, blood perfusion through the skin in terms of amount and closeness of approach to the skin s surface is regulated by its temperature and also by an individual s need to maintain the body s 37° C isothermal state. Since clearance of percuta-neously absorbed drug to the systemic circulation is sensitive to blood flow, a fluctuation in blood flow might be expected to alter the uptake of chemicals. No clear-cut evidence exists that this is so, however, which seems to teach us that even the reduced blood flow of chilled skin is adequate to efficiently clear compounds from the underside of the epidermis. [Pg.209]

A hydrostatic stress can be superposed, but it is caused only by elastic volumetric strain of the composite. The result in Eqn. (39) is, perhaps, not very useful since it is rare that a steady strain rate will be kinematically imposed. When both fiber and matrix creep, the steady solutions for a fixed stress in isothermal states are quite complex but can be computed by numerical inversion of Eqn. (39). The solution can, however, be given for the isothermal case where the fibers do not creep. (For non-fiber composites, this should be... [Pg.314]

For polystyrene, D = 83 SOOg.mol i, which means that beyond a mass of approximately D, the temperature T is fixed - (T ) = 49.7 0.3°C.Therefore, in the entangled region, the free volume fraction is constant at a given temperature and the iso-free volume state merges into the isothermal state. [Pg.131]

The theorem derived above refers to equilibrium states at constant pressure an exactly similar discussion of isothermal states leads to the second theorem which may be stated in the form ... [Pg.282]

Note that setting A = 1 reduces the isentropic state to the isothermal state). For isentropic compression. [Pg.452]

Another factor to be considered is the thermal state of the system. In practice, an effort is usually made to work with isothermal systems however, if the reaction of interest is sufficiently exothermic, it may be impossible to maintain an isothermal state. In the extreme case of rapid exothermic reactions, e.g., flames, explosions, etc., the system is best described as adiabatic rather than isothermal. [Pg.2]

In this case of irreversible isotherm, the initial concentration Cj inside the particle must be zero otherwise for finite Cj (no matter how small it is) the irreversible adsorption isotherm states that the adsorbed phase (f(Cj) = C ) is completely saturated. Hence no adsorption kinetics will happen no matter what the initial bulk phase concentration is. [Pg.801]

The Gibbs isotherm states that the adsorption of surfactants leads to a decrease of the interfacial tension y. However, the interfacial tension y will not completely vanish as long as the particulate and fluid phase can be distinguished. [Pg.80]

To keep the reactor in an isothermal state, the heat liberated due to exothermic reaction has to be continuously exchanged. This heat exchange rate Q is... [Pg.193]

Figure 12.3 Isochoric heat capacities Cy for propane as a function of temperature T obtained from the equation of state of Lemmon et alf Isobars are shown at pressures of (0, 1,2, 3,4, 5, 6, 8,10, 20, 50,100, 200, 500,1000 and 2000) MPa. The melting line is shown intersecting the liquid phase isotherms. State points below the melting line are extrapolations of the liquid phase to very low temperatures. Figure 12.3 Isochoric heat capacities Cy for propane as a function of temperature T obtained from the equation of state of Lemmon et alf Isobars are shown at pressures of (0, 1,2, 3,4, 5, 6, 8,10, 20, 50,100, 200, 500,1000 and 2000) MPa. The melting line is shown intersecting the liquid phase isotherms. State points below the melting line are extrapolations of the liquid phase to very low temperatures.
The advantage of the radial turbo compressors is, apart from their reliability and compact design, their high efficiency The compression process comes quite close to an isothermal state change, because the gas is cooled between subsequent compression stages. And the ideal isothermal compression is known... [Pg.46]

An HR system must be in a state of thermal equilibrium, which means that heat losses must be compensated for by heating. In the ideal case, an HR system will be in an isothermic state. [Pg.205]

Eq. (8.22) can be used for predicting a certain temperature profile for given values of both flow rates F and F. In some processes, a certain temperature profile in time is desired. By substituting F as a function of time in eq. (8.22), it is possible to find a feeding programme for obtaining the desired temperature profile. In most processes, however, the temperature has to be kept constant. By putting dTIdt = 0 one finds the relation between F and F for the isothermal state. [Pg.236]

Assume an isothermal state where anhydrite, decahydrate and water vapour are in mutual equilibrium, i.e. [Pg.189]

The Gibbs isotherm states that, in an ideal (very dilute) solution ... [Pg.402]


See other pages where Isothermal state is mentioned: [Pg.259]    [Pg.61]    [Pg.50]    [Pg.156]    [Pg.192]    [Pg.154]    [Pg.88]    [Pg.158]    [Pg.255]    [Pg.360]    [Pg.248]   
See also in sourсe #XX -- [ Pg.71 ]

See also in sourсe #XX -- [ Pg.33 ]




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Adsorption Isotherms from Two-Dimensional Equations of State

Equation of state and adsorption isotherms

Formal theories of isothermal solid state decompositions

Isotherm steady state

Isothermal change of state

Isothermal compression - Equations of state

Isothermal corresponding-states correlation

Isothermal reactors unsteady-state operation

Isothermal solid state reactions

Isotherms Derived from the Equation of State

Mechanism of Isothermal Reaction in Solid State

Multiple steady states isothermal

Series Solutions for Non-isothermal Catalyst Pellet - Multiple Steady States

Solid-state reactions isothermal kinetic rate equation

Steady State Models for Isothermal Heterogeneous Distributed Systems

Steady State Models for Isothermal Heterogeneous Lumped Systems

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