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Phase contact

The existence of Galvani potentials between two different conducting phases is connected with the formation of an electric double layer (EDL) at the phase boundary (i.e., of two parallel layers of charges with opposite signs, each on the surface of one of the contacting phases). It is a special feature of such an EDL that the two layers forming the double layer are a very small (molecular) distance apart, between 0.1 and 0.4nm. For this reason EDL capacitances are very high (i.e., tenths of pF/cm ). [Pg.25]

Usually g-J(ion) 7 Aj I and J(dip) / Aj/. This is caused by mutual influence of the contacting phases on the orientation of dipolar molecules in the interfacial zone. [Pg.20]

Covers charging due to relative motion or separation of two contacting phases in the absence of external electrostatic fields, radiation, or thermionic emission. The superimposition of such effects may serve to confuse the data in many cases, especially those involving natural phenomena. [Pg.56]

Fig. 4-6. llie inner potential, 4, and the outer potential, tf, of two condensed phases A and B before and after their contact d4 )= inner (outer) potential difference between two contacting phases o = surface or interface charge dip = surface or interface dipole. [Pg.91]

An electrostatic potential difference, called the inner potential difference, arises across the interface of two contacting phases. This inner potential difference consists of a potential gA/ac) due to an interfacial charge (charge on both sides of the interface), Oa/b> aiid a potential gj /snip) due to an interfacial dipole, dipA/B, as shown in Eqn. 4-3 ... [Pg.92]

Obviously, the interfacial charge differs from the initial (before contact) surface charges oa and ob (oa/b " Oa + ob) and the interfacial dipole dipA/s is not the same as the arithmetic sum of the initial surface dipoles igtjaibt) XA(dip)-Xadip)) Thus, it follows that both the inner and the outer potential differences, A( >a/b and Ai a , between the two contacting phases are not the same as those and Atp A/B before the contact. As a result, Eqn. 4-2 yields Eqn. 4-4 ... [Pg.92]

The inner potential difference between two contacting phases is cafied in electrochemistry the Galvani potential difference, and the outer potential difference is called the Volta potential difference. The outer potential difference corresponds to what is called the contact potential between the two phases. We call, in this test, the inner potential difference across an interface the interfacial potential. [Pg.92]

The outer potential difference between two contacting phases can be measured because it is a potential difference between two points in the same vacuum or gas phase outside the free surfaces of the two phases. On the other hand, the inner potential difference can not be measured, because the potential measuring probe introduces its interfacial potential that differs with the two phases and thus can not be canceled out this gives rise to an unknown potential in the potential measurement. [Pg.92]

This leads to the Helmholtz model of the interface (Fig. 10.5) when the other contacting phase is a metal. The Helmholtz model of the interface predicts that the value of the double layer capacity (Q,) will be given by ... [Pg.271]

The relationship between current and overpotential at the non-blocking interface is generally dependent on both the interface structure and the number of mobile species in the contacting phases. The simplest situation is that represented by an interface of the type Ag/Ag4Rbl5 where (i) the Helmoltz model of the interface is appropriate and (ii) there is only one mobile species in the electrolyte (Ag" ). In this case the relationship between i and is a linear one at low values of rj (rj < 10 mV) ... [Pg.278]

For the chemical reactor, the researchers used a nanoparticle catalyst deposited on metallic micro-structured foils. They tested Cu/ZnO and Pd/ZnO catalysts deposited on the microstructured foils. The Cu/ZnO catalyst was more active than the Pd/ZnO catalyst and had a lower selectivity to undesired carbon monoxide. However, because the Pd/ZnO catalyst was more stable, it was selected for use in their fuel processor. The Pd/ZnO carbon monoxide selectivity of the powder catalyst pressed into a pellet was lower than that of the nanoparticle catalyst deposited on the microstructured foils. This effect was attributed to contact phases between the catalyst and the metal foils. ... [Pg.545]

Fig. 4.9. The arrangement of contacting phases in an ISFET. Vq denotes the gate voltage. Fig. 4.9. The arrangement of contacting phases in an ISFET. Vq denotes the gate voltage.
The most useful method of measuring surface tension is by the well-known Wilhelmy plate method. If a plate-shaped metal is dipped in a liquid, the surface tension forces will be found to produce a tangential force (Figure 2.13). This is because a new contact phase is created between the plate and the liquid. [Pg.27]

All types of contactors—trickle beds, slurry reactors, and fluidized beds—can be treated at the same time. What is important is to recognize the flow patterns of the contacting phases and which component, A or B, is in excess. First consider an excess of B. Here the flow pattern of liquid is not important. We only have to consider the flow pattern of the gas phase. So we have the following cases. [Pg.503]

At equilibrium between each contacting phases for the common constituents... [Pg.9]

It inhibits plasmin and kallikrein, thus directly affecting fibrinolysis. It also inhibits the contact phase activation of coagulation which both initiates coagulation and promotes fibrinolysis. [Pg.242]

The reason for the disparity in performance of such devices in the two services has been clearly outlined by Hachmuth (HI). Bubble-tray towers for distillation, for example, use as the source of energy for dispersion of the gas and for developing the desirable turbulent flow conditions both the expansion of the vapor as it experiences a pressure drop in flowing through the tray, and the liquid head available between trays. In liquid extraction only the liquid head is available. When it is considered that the difference in densities of the contacted phases in distillation may be of the order of 50 to 60 lb./cu. ft., whereas in extraction it is more likely to be of the order of 5 or less, it is easy to understand that in the latter case there is simply insufficient energy available from this source to provide for adequate dispersion and interphase movement. Interfacial area between phases remains small, turbulences developed are of a low order, and mass transfer rates are disappointingly small. [Pg.290]

In general, the forces which contribute to the net force exerted on the tip can be divided into three groups ( Fig. lb) (i) surface forces, Fs, (ii) forces due to the sample deformation, Fd> and (iii) the deflection force of the cantilever, Fc. It is important to note that all three forces can be of either sign. The van der Waals force is determined by the Hamaker constant, which depending on the dielectric properties of the contacting phases can be positive or negative. Also the deformation force can be repulsive or attractive, when the sample is pressed or stretched by the tip, respectively. [Pg.68]

Nonisothermal systems are accounted for by the introduction of temperature-control units into the generic reactor unit representation. These units consist of elements associated with the manipulation of temperature changes and constitute temperature profiles (profile-based approach) and heaters/coolers (unit-based approach). The assumption of thermal equilibrium between the contacting phases reduces the need for a single temperature per shadow reactor compartment. The profile-based system (PBS) finds the optimum profiles without considering the details of heat transfer mechanisms. Because the profiles are imposed rather than... [Pg.429]

Membrane contactors are systems in which the membrane function is to facilitate diffusive mass transfer between two contacting phases (liquid-liquid, liquid-gas, etc.) without dispersion of one phase within another [12]. The membrane does not act as a selective barrier, but creates and sustains the interfaces immobilized at the... [Pg.267]

For chemical reactions involving charged species in multiple (but contacting) phases, the condition for equilibrium is, in analogy to Eq. (30) of Chapter 7,... [Pg.301]

Mineral grinding leads to distorsion of chemical and ionic bonds between atoms and ions. In the fracture areas binding and coordination states get asymmetric, and new electron and electric valences occur. Spontaneous reactions in the crystalline structure and with contact phases are the consequence of the distorsion. Surface distorsion of the crystalline structure may be diminished or completely abolished. At the same time, the free surface energy decreases due to polarization of surface ions. These ions are redistributed in the inner or outer layer of the crystalline surface and/or due to chemisorption of molecules and ions1. All these changes occur side by side, but one of them can suppress the effect of the others in a decisive manner. [Pg.93]

Most chemical compounds are characterised by diffusion of the components across the bulks of their growing layers in the form of atoms or ions. The process of bulk diffusion is described by Fick s laws. The first Fick law relates the flux of atoms of a given component to its diffusion coefficient and concentration gradient in the direction of diffusion at constant surface area of contacting phases ... [Pg.57]

Reactive absorption is usually carried out in apparata providing a continuous flow of both contacting phases. Reactive absorption units can be best classified if one considers which of the phases is in a continuous form, and which is in a disperse form. Using this criterion, the classification of the reactive absorption equipment is represented in Tab. 9.2 (see Ref. [1]). [Pg.267]


See other pages where Phase contact is mentioned: [Pg.130]    [Pg.112]    [Pg.600]    [Pg.18]    [Pg.167]    [Pg.352]    [Pg.30]    [Pg.90]    [Pg.93]    [Pg.269]    [Pg.276]    [Pg.163]    [Pg.383]    [Pg.393]    [Pg.297]    [Pg.198]    [Pg.256]    [Pg.859]    [Pg.269]    [Pg.429]    [Pg.141]    [Pg.3]    [Pg.45]    [Pg.397]    [Pg.272]    [Pg.331]   
See also in sourсe #XX -- [ Pg.855 ]




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Classification of Microreactors - Phase-contacting Principles

Contact Between Three Phases Wetting

Contact angle mobile phase velocity

Contact of phases

Contact phase proteinases

Contact-phase activation

Contacting with Continuous Phases

Contacting with Disperse Phases

Disperse phase contact

Equilibrium of a Species Between Two Phases in Contact

Liquid Phase Contact

Liquid phase sintering contact flattening

Liquid-solid phase-contacting principles

Mechanical contact vapor-phase

Phase Contacts between Particles in Disperse Structures

Phase contact line

Phase contact ratio

Phase contact structures

Phase contact structures chemical modifiers

Phase contact structures mechanical stresses

Phase contact structures particle bridging

Phase contact structures silica particles

Phase contact systems

Phase contacting

Phase contacting

Phase contacting conditions

Phases contact time behaviour

Potential difference between two contacting phases

Reaction phase-contacting principles

Rules of Thumb about the Context for a Chemical Process Heterogenous Phase contacting

Stationary phases contact angle

Structures with Phase Contacts

Surface force three-phase contact line

Surface state contacting phase

Three-Phase Contact Line Wetting

Three-phase contact

Three-phase contact extension

Three-phase contact line

Three-phase contact line wetting front

Three-phase contact wetting perimeter

Three-phase contacting

Three-phase line/perimeter, contact

Three-phase line/perimeter, contact angle

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