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Optimal temperature

The temperature (or salinity) at which = o mt called the optimal temperature (or optimal salinity), because at that temperature (or salinity) the... [Pg.151]

Each blood component has specific storage requirements in terms of optimal temperature, additives, expiration, and storage containers. Red blood cells (RBC) from whole blood, provided in 200 mL units, have an expiration of 42 days. Fro2en, deglycerolized RBC, in 170 mL containers, and washed red cells, in 200 mL containers, both expire 24 hours after thawing and washing, respectively leukocyte-reduced RBC, in 200 mL containers, are viable for 24 hours. [Pg.524]

Sulfur generally becomes SO2, although some smaller amounts are possibly converted to SO, depending on temperature. Chlorine mosdy results in HCl, but some CI2 and atomic Cl forms as well. Any atomic Cl recombines to form CI2 if quenching is rapid. Low incineration temperatures favor CI2, and high temperatures favor atomic Cl. There is an optimal temperature for minimising the total effective CI2, ie, CI2 + Cl/2. [Pg.58]

Table 6. Optimal Temperature Range of Conventional Catalyst Systems for Unsaturated Polyesters... Table 6. Optimal Temperature Range of Conventional Catalyst Systems for Unsaturated Polyesters...
Optimizing Temperature. Temperature is usually dictated by yield considerations. The choice of temperature for yield often overrides any desire to choose a temperature that minimizes the energy bill. [Pg.83]

CSTBs—minimum volume of battery, maximum yield, optimal temperature for reversible reaction, minimum total cost, reactor volume with recycle, maximum profit for reversible reaction with recycle, and heat loss... [Pg.706]

Enzyme reac tions are also sensitive to pH and temperature changes. In characterizing an enzyme, its optimal pH and optimal temperature are conditions at which the enzyme has its highest catalytic activity. [Pg.2149]

Adesina [14] considered the four main types of reactions for variable density conditions. It was shown that if the sums of the orders of the reactants and products are the same, then the OTP path is independent of the density parameter, implying that the ideal reactor size would be the same as no change in density. The optimal rate behavior with respect to T and the optimal temperature progression (T p ) have important roles in the design and operation of reactors performing reversible, exothermic reactions. Examples include the oxidation of SO2 to SO3 and the synthesis of NH3 and methanol CH3OH. [Pg.543]

The feed temperature (Tq) for the adiabatie operation at the optimal temperature T p. ... [Pg.548]

The optimal temperature range for the fluorination process was found to be about 230-290°C. The resulting cake was leached with water. The prepared solution was separated from the precipitate by regular filtration and the separated insoluble precipitate was identified as lithium fluoride, LiF. The solution contained up to 90 g/1 Ta205. Solution acidity was relatively low, with a typical pH = 3-4, and was suitable for the precipitation of potassium heptafluorotantalate, K2TaF7, tantalum hydroxide or further purification by liquid-liquid extraction after appropriate adjustment of the solution acidity [113]. [Pg.264]

The optimal temperature range for the interaction was found to be 150-230°C. The cake resulting from the fluorination process was also successfully leached with water, dissolving ammonium oxyfluoroniobate, (NH4)3NbOF6. The solution was separated from the precipitate of lithium fluoride. The main parameters of the solution were a niobium concentration of about 75 g/1 Nb205, pH = 3—4. [Pg.264]

It can be seen from Figure 5 that the amount of the added synergist Sb203 of the flame retardant strongly effects the PBDF yield and the optimal temperature of PBDF formation. The kind of polymeric matrix itself does not effect yields of PBDF. [Pg.371]

This chapter treats the effects of temperature on the three types of ideal reactors batch, piston flow, and continuous-flow stirred tank. Three major questions in reactor design are addressed. What is the optimal temperature for a reaction How can this temperature be achieved or at least approximated in practice How can results from the laboratory or pilot plant be scaled up ... [Pg.151]

Reaction rates almost always increase with temperature. Thus, the best temperature for a single, irreversible reaction, whether elementary or complex, is the highest possible temperature. Practical reactor designs must consider limitations of materials of construction and economic tradeoffs between heating costs and yield, but there is no optimal temperature from a strictly kinetic viewpoint. Of course, at sufficiently high temperatures, a competitive reaction or reversibility will emerge. [Pg.154]

Multiple reactions, and reversible reactions, since these are a special form of multiple reactions, usually exhibit an optimal temperature with respect to the yield of a desired product. The reaction energetics are not trivial, even if the... [Pg.154]

Differentiation and setting dbout/dT = 0 gives a transcendental equation in Toptimai that cannot be solved in closed form. The optimal temperature must be found numerically. [Pg.155]

The results of Example 5.2 apply to a reactor with a fixed reaction time, i or thatch- Equation (5.5) shows that the optimal temperature in a CSTR decreases as the mean residence time increases. This is also true for a PFR or a batch reactor. There is no interior optimum with respect to reaction time for a single, reversible reaction. When Ef < Ef, the best yield is obtained in a large reactor operating at low temperature. Obviously, the kinetic model ceases to apply when the reactants freeze. More realistically, capital and operating costs impose constraints on the design. [Pg.156]

Example 6.5 Find the optimal temperature profile, T z), that maximizes the concentration of component B in the competitive reaction sequence of Equation (6.1) for a piston flow reactor subject to the constraint that F=3h. [Pg.199]

FIGURE 6.2 Piecewise-constant approximations to an optimal temperature profile for consecutive reactions (a) 10-zone optimization (b) 99-zone optimization. [Pg.201]

Compare the (unconstrained) optimal temperature profiles of 10-zone PFRs for the following cases where (a) the reactions are consecutive as per Equation (6.1) and endothermic (b) the reactions are consecutive and exothermic (c) the reactions are competitive as per Equation (6.6) and endothermic and (d) the reactions are competitive and exothermic. [Pg.204]

Can the calculus of variations be used to find the optimal temperature profile in Example 6.5 ... [Pg.205]

Fig. 5. Effective g assignment of the low-field S = IEPR signals in D. vulgaris Fepr protein [from 11)]. The spectrum was recorded at the optimEd temperature of 12 K, that is, at which the amplitude is maximal and lifetime broadening is not significEmt. EPR conditions microwave frequency, 9.33 GHz microwave power, 80 mW modulation amplitude, 0.8 mT. Fig. 5. Effective g assignment of the low-field S = IEPR signals in D. vulgaris Fepr protein [from 11)]. The spectrum was recorded at the optimEd temperature of 12 K, that is, at which the amplitude is maximal and lifetime broadening is not significEmt. EPR conditions microwave frequency, 9.33 GHz microwave power, 80 mW modulation amplitude, 0.8 mT.
Eqs. (1) and (7) will be used to derive optimal temperature policies. [Pg.324]

In Figme 4 is shown the effect of initiator half-life for an initiation activation energy of 120 KJ/mol on the optimum temperature and optimum time. It can be seen that the optimum temperature is almost independent of the half-life. As expected, the optimum time increases with an increase in half-life. Closer study of the results reveals that an almost constant optimal temperature is due to high NL, Values. A much higher temperature would cause to be higher than the desired Mf. [Pg.327]

These simulations clearly reveal the importance of considering M, in calculating the optimal temperature. is dependent on the heat of polymerization (-AH) as given by Eq. (13). Most monomers have heats of polymerization in the range of 50 to 80 KJ/mol. We thus decided to study the effect of (-AH) on optimal temperature and time for various half-life values of the initiator. The results are shown in Figme 5. [Pg.327]

Figure 5. Effect of Heat of Polymerization on Optimal Temperature and Time for Initiator with 10 hour half life at marked T. Figure 5. Effect of Heat of Polymerization on Optimal Temperature and Time for Initiator with 10 hour half life at marked T.
HPA catalyzed nitration of toluene was summarized in Table 1 and 2. The optimal temperature... [Pg.355]

In comparison with hydrocarbon and polymeric matrices, which have their own absorptions in the IR and can react chemically with the intermediates, inert gas matrices are free of these shortcomings. Neon, krypton and xenon have been used as matrix substances in some studies. However, only argon and nitrogen matrices are widely adopted because of the availability of the pure gases and the fact that there is a variety of cryostats that can provide the optimal temperature conditions for the formation of rigid and transparent matrices from these elements. [Pg.2]


See other pages where Optimal temperature is mentioned: [Pg.151]    [Pg.304]    [Pg.475]    [Pg.171]    [Pg.303]    [Pg.379]    [Pg.21]    [Pg.547]    [Pg.663]    [Pg.72]    [Pg.154]    [Pg.436]    [Pg.560]    [Pg.321]    [Pg.323]    [Pg.327]    [Pg.335]    [Pg.335]   
See also in sourсe #XX -- [ Pg.183 ]




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Temperature optimization

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