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Dissipation operator

The specific entropy of a solvent increases with the solute concentration, and if the input solvent is the same, inequality (5.70) yields Ac1 > Ac2, and hence Eq. (5.69) shows that Q < Q2. This means that the solvent flow rate is smaller in the less dissipative operation, and the solvent at the outlet is more concentrated. That is, the operating conditions of solvent determine the less dissipative operation. Whether this optimum is an overall economic optimum will depend mainly on the cost of the technology. [Pg.290]

The first situation we wish to consider concerns the error bounds in the spectral density of a pure dissipation operator T, whose eigenvalues y = ( in 0) lie on the negative imaginary axis. Consider the equation of motion of the type... [Pg.125]

Another situation in which error bounds can be provided is in the calculation of a correlation function of a piuely dissipative operator (eigenvalues = —1 , > 0, on the negative imaginary axis), earlier discussed in this... [Pg.128]

Thus for the calculation of error bounds in the correlation function associated to a pure dissipative operator, we can exploit the properties summarized by Eq. (8.11). [Pg.128]

In the first section, the time rate of energy dissipation for a damped oscillator is introduced by the Rayleigh dissipation potential. The quantum version of this quantity, i.e., the time rate of the energy dissipation operator, can be originated from Equation (14) as... [Pg.62]

We finally mention that the system/bath picture for studying the pyrazine spectrum has been adopted by two other publications. There, however, the bath was treated implicitly by dissipative operators of the Lindblad type. [Pg.613]

D being a suitable dissipative operator [17,18]. For simplicity of notation, D is written as a time-independent operator. Upon the substitution Dp t) D t — f)p t ),... [Pg.451]

Ordinarily, for purposes of evaluation, the applied force is taken to be small enough that, throughout the entire process, the system deviates only very slightly from prevailing equilibrium conditions. This ensures slow implementation of the process and rules out turbulent or dissipative operations whose description would otherwise require a whole host of extrathermodynamic variables. Nevertheless, we will later take up cases where the applied force does exceed that needed for guaranteeing reversibility. [Pg.22]

The laser normally operates in the pulsed mode because of the necessity of the dissipation of a large amount of heat between pulses. [Pg.347]

In addition to the previously noted safety factors associated with these processes, there are additional needs for dust control and ventilation for dissipation of various vapors from pressing, tempering/heat treatment, and machining and finishing operations. [Pg.390]

The pulsed-plate column is typically fitted with hori2ontal perforated plates or sieve plates which occupy the entire cross section of the column. The total free area of the plate is about 20—25%. The columns ate generally operated at frequencies of 1.5 to 4 H2 with ampHtudes 0.63 to 2.5 cm. The energy dissipated by the pulsations increases both the turbulence and the interfacial areas and greatly improves the mass-transfer efficiency compared to that of an unpulsed column. Pulsed-plate columns in diameters of up to 1.0 m or mote ate widely used in the nuclear industry (139,140). [Pg.75]

Ferrites aHowing for operation at frequencies well above 1 MH2 have also become available, eg, 3F4 and 4F1 (Table 6). Other newer industrial power ferrites are the Siemens-Matsushita N-series (28,97) the TDK PC-series (28,100), and the Thomson B-series (28,103). While moving to higher frequencies, the ferrites have been optimized for different loss contributions, eg, hysteresis losses, eddy current losses, and resonance losses. Loss levels are specified at 100°C because ambient temperature in power appHcations is about 60°C plus an increase caused by internal heat dissipation of about 40°C. [Pg.197]

Electrically conductive mbber (13) can be achieved by incorporation of conductive fillers, eg, use of carbon or metal powders. These mbbers exhibit volume resistivities as low as lO " H-cm. Apphcations include use in dissipation of static charge and in conductive bridging between dissimilar electronic materials under harsh operating conditions. [Pg.401]

Heating elements operating <760°C are almost always of a chrome—nickel resistance alloy and are ia the form of ribbon, cast alloy, open wire cods, or sheathed constmction. Several alloys are suitable ia this temperature range and all are satisfactory if properly appHed. In general, the more expensive alloys are used when physical space limitations dictate higher watts per area dissipation from the element. [Pg.136]

A case provides mechanical support and protection for the devices, interconnects, and substrate mounted in it it also helps to dissipate heat during component operation and offers protection to the contents of the package from environmental stresses, contaminants, and, in the case of hermetic packages, moisture. [Pg.530]

Another resonant frequency instmment is the TA Instmments dynamic mechanical analy2er (DMA). A bar-like specimen is clamped between two pivoted arms and sinusoidally oscillated at its resonant frequency with an ampHtude selected by the operator. An amount of energy equal to that dissipated by the specimen is added on each cycle to maintain a constant ampHtude. The flexural modulus, E is calculated from the resonant frequency, and the makeup energy represents a damping function, which can be related to the loss modulus, E". A newer version of this instmment, the TA Instmments 983 DMA, can also make measurements at fixed frequencies as weU as creep and stress—relaxation measurements. [Pg.199]

The most common thickener is the circular basin type shown in Figure 7. After treatment with flocculant, the feed stream enters the central feed well which dissipates the stream s kinetic energy and disperses it gendy into the thickener. The feed finds its height in the basin where its density matches the density of the inside suspension and spreads out at that level. SoHds concentration increases downward in an operating thickener giving stabiHty to the process. [Pg.322]


See other pages where Dissipation operator is mentioned: [Pg.238]    [Pg.69]    [Pg.251]    [Pg.1342]    [Pg.451]    [Pg.238]    [Pg.69]    [Pg.251]    [Pg.1342]    [Pg.451]    [Pg.2249]    [Pg.2487]    [Pg.129]    [Pg.80]    [Pg.1]    [Pg.100]    [Pg.47]    [Pg.379]    [Pg.379]    [Pg.380]    [Pg.457]    [Pg.253]    [Pg.340]    [Pg.528]    [Pg.483]    [Pg.111]    [Pg.5]    [Pg.36]    [Pg.176]    [Pg.177]    [Pg.353]    [Pg.354]    [Pg.106]    [Pg.316]    [Pg.172]    [Pg.86]   
See also in sourсe #XX -- [ Pg.125 ]




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