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Mass balance relationships

It is often experimentally convenient to use an analytical method that provides an instrumental signal that is proportional to concentration, rather than providing an absolute concentration, and such methods readily yield the ratio clc°. Solution absorbance, fluorescence intensity, and conductance are examples of this type of instrument response. The requirements are that the reactants and products both give a signal that is directly proportional to their concentrations and that there be an experimentally usable change in the observed property as the reactants are transformed into the products. We take absorption spectroscopy as an example, so that Beer s law is the functional relationship between absorbance and concentration. Let A be the reactant and Z the product. We then require that Ea ez, where e signifies a molar absorptivity. As initial conditions (t = 0) we set Ca = ca and cz = 0. The mass balance relationship Eq. (2-47) relates Ca and cz, where c is the product concentration at infinity time, that is, when the reaction is essentially complete. [Pg.34]

The mass balance relationships for the feed plate, the plates in the stripping section, of the column and for the reboiler must, however, be modified, owing to the continuous feed to the column and the continuous withdrawal of bottom product from the reboiler. The feed is defined by its mass flow rate, F, its composition xp and the thermal quality or q-factor, q. The column bottom product is defined by its mass flow rate, W, and composition, xw and is controlled to maintain constant liquid level in the reboiler. [Pg.209]

The IC50 can thus be accurately determined by fitting the concentration-response data to Equation (5.1) through nonlinear curve-fitting methods. Some investigators prefer to plot data in terms of % inhibition rather than fractional activity. Using the mass-balance relationships discussed above, we can easily recast Equation (5.1) as follows ... [Pg.114]

Again, we have mass balance relationships that provide three equations (C, H, O balance) and one free variable. [Pg.323]

For fed-batch fermentation, the model equations need to include the continuous feeding of sterile substrate to the fermenter, but zero outflow. The increase in volume (total accumulation of mass) that occurs in the fermenter due to the feeding is represented by a total mass balance relationship. [Pg.538]

Since the burning rate of a propellant is dependent on the burning pressure, the mass balance between the mass generation rate in the chamber and the mass discharge rate from the nozzle is determined by the pressure. In addition, the propellant burning rate in a rocket motor is affected by various phenomena that influence the mass balance relationship. Fig. 14.4 shows typical combustion phenomena encountered in a rocket motor, from pressure build-up by ignition to pressure decay upon completion of the combustion. [Pg.406]

Using this equation, together with a mass balance relationship ([E] = [E]t - [ES]), we can solve for [ES]/[E]t, the fraction of enzyme combined as enzyme-substrate complex (Eq. 9-18). [Pg.459]

Equation (3.4) describes the mass balance relationship for one of the reactions being studied. It is also valid if the chamber is perfectly mixed or... [Pg.54]

Atmospheric Aerosol Sulfate. Isotope measurements of non-seasalt sulfate in marine aerosols (24.52.631 require that sulfate from sea spray be either physically or mathematically removed from the sample medium. Mathematically, mass balance relationships are used to correct the value for the presence of seasalt sulfate in the sample. Physical means employ impactors or cyclone separators to segregate particles based on size so that value for non-seasalt sulfate can be directly measured. [Pg.375]

These approaches place particular emphasis on the spatial aspects of the drug absorption from the gastrointestinal tract. The small intestine is assumed to be a cylindrical tube with fixed dimensions where the drug solution or suspension follows a homogeneous flow. Mass balance relationships under steady-state as-... [Pg.117]

Irrespective of the specific case considered, the general mass balance relationship for the system depicted in Figure 6.2 under the steady-state assumption... [Pg.118]

Magnetic moment, 153, 155, 160 Magnetic quantum number, 153 Magnetization, 160 Magnetogyric ratio, 153, 160 Main reaction, 237 Marcus equation, 227, 238, 314 Marcus plot, slope of, 227, 354 Marcus theory, applicability of, 358 reactivity-selectivity principle and, 375 Mass, reduced, 189, 294 Mass action law, 11, 60, 125, 428 Mass balance relationships, 19, 21, 34, 60, 64, 67, 89, 103, 140, 147 Maximum velocity, enzyme-catalyzed, 103 Mean, harmonic, 370 Mechanism classification of. 8 definition of, 3 study of, 6, 115 Medium effects, 385, 418, 420 physical theories of, 405 Meisenheimer eomplex, 129 Menschutkin reaction, 404, 407, 422 Mesomerism, 323 Method of residuals, 73 Michaelis constant, 103 Michaelis—Menten equation, 103 Microscopic reversibility, 125... [Pg.245]

In view of the mass balance relationship Ca = Ca + Cz, this leads to Eq. (2-11), which can also be obtained from Eq. (2-6). [Pg.265]

Katz B. G., Bricker O. P., and Kennedy M. M. (1985) Geochemical mass-balance relationships for selected ions in precipitation and stream water, Catoctin Mountains, Maryland. Am. J. Sci. 285, 931 —962. [Pg.2385]

In equation 11, v=[ML]/Cl, and all other symbols used are the same as defined previously for nonlinear and modified Stem-Volmer models. Theoretically, a plot of v versus v/[L] should yield a straight line with K as the y intercept and -K as the slope. Algebraic manipulation of Cl and mass balance relationships (equations 4 and 5) and substitution into equation 11, yields equation 12. [Pg.115]

Mass-balance relationships completely analogous to equation (3.1) can be derived for the rapidly and slowly perfused tissue. [Pg.38]

Zone-B Solubility of the Weak Acid audits Salt Under Equilibrium Conditions Inside of the pH region enclosed by the limits of Zone-B, one hnds both the free acid and its salt form. The mass balance relationship in this zone defines the total solubility (Sj) at any particular pH value as the sum of the concentration of the free acid plus the concentration of its salt form ... [Pg.46]

The reactor performance is described by the following mass balance relationships ... [Pg.61]


See other pages where Mass balance relationships is mentioned: [Pg.175]    [Pg.19]    [Pg.60]    [Pg.67]    [Pg.89]    [Pg.100]    [Pg.205]    [Pg.33]    [Pg.32]    [Pg.35]    [Pg.287]    [Pg.77]    [Pg.10]    [Pg.175]    [Pg.121]    [Pg.122]    [Pg.38]    [Pg.58]    [Pg.289]    [Pg.300]    [Pg.771]    [Pg.121]    [Pg.68]    [Pg.206]   
See also in sourсe #XX -- [ Pg.19 , Pg.21 , Pg.34 , Pg.60 , Pg.64 , Pg.67 , Pg.89 , Pg.103 , Pg.140 , Pg.147 ]




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Mass balance

Mass balancing

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