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Coolant temperature, effect

The effect on the coolant temperature of latent and sensible heat transferred to the surface from the condensing vapor is as shown in equation 5 ... [Pg.95]

Temperature control is unlikely to be effective for condensers, unless the liquid stream is sub-cooled. Pressure control is often used, as shown in Figure 5.17d, or control can be based on the outlet coolant temperature. [Pg.230]

A well stirred reactor is effecting a first order exothermic reaction with heat transfer under the following conditions x = 1 min Cf = 1 mol/liter Tf = 350, feed temperature Tm = 350, coolant temperature k - exp(25-10000/T), 1/min UA/pVrCp = 1/min AHr/pCp = -200 °K liter/mol Find the steady operating conditions. [Pg.460]

The size and complexity of the N-reactor plant and the limited amount of computing equipment that was available necessitated a judicious use of simplifying assumptions. For instance, primary coolant temperature transport lags were lumped into two groups, one each for the hot and cold loop legs thermodynamic effects in the secondary system condensate headers and surge... [Pg.226]

The idea behind the proposed feedback is the estimation of the generated heat by reaction, then simulations are aimed to show how the reactor temperature stabilization is affected by the initial value of the estimated heat, 7(0). Figure 4 shows the reactor temperature and the computed coolant temperature for several initial values >)(0). Here the estimation parameter was arbitrarily chosen L = 0.5. Note that as the estimated value decreases the convergence to the reference temperature, 283 K, is reached. Figure 5 shows the same effect for the value of the estimation parameter L = 5.0. By comparing both Figures 4 and 5, we can observe that as the value of L increases... [Pg.47]

Fig. 4. Effects of the estimated initial value of the reaction heat for L = 0.5. Dotted-line, 7(0) = 10.0 Solid-line, r)(0) = 5.0 Dash-dotted line, 17(0) = 1.0 Dashed-line, (0) = 0.0. Smaller initial values of the heat reaction lead to better performance than large values, a) Reactor temperature and b) coolant temperature. Fig. 4. Effects of the estimated initial value of the reaction heat for L = 0.5. Dotted-line, 7(0) = 10.0 Solid-line, r)(0) = 5.0 Dash-dotted line, 17(0) = 1.0 Dashed-line, (0) = 0.0. Smaller initial values of the heat reaction lead to better performance than large values, a) Reactor temperature and b) coolant temperature.
Fig. 6. Effect of increasing the high gain parameter L on the performance of the control action. The response of the coolant temperature is faster as L increases. However, a very large value of L can induce overshot and saturation. On contrary, a very low value on L can induce off set at steady state. The arrow in picture indicates the direction of the effect that is, L was increased as the arrow direction shows. Fig. 6. Effect of increasing the high gain parameter L on the performance of the control action. The response of the coolant temperature is faster as L increases. However, a very large value of L can induce overshot and saturation. On contrary, a very low value on L can induce off set at steady state. The arrow in picture indicates the direction of the effect that is, L was increased as the arrow direction shows.
We used the wall temperature in the boundary condition, and this may be different from the coolant temperature T. There may be temperature variations across the wall as well as through the coolant. These are described through the overall heat transfer coefficient U, but in practice all these effects must be considered for a detailed description of the wall-cooled tubular reactor. [Pg.240]

To be effective, the carrier gas must fulfill two requirements. First, it cannot be adsorbed at the coolant temperature second, it must possess a thermal conductivity sufficiently different from that of the adsorbate that small concentration changes can be detected. [Pg.162]

Figure 2.46 Effect of coolant temperature on CO conversion for the water-gas shift reaction in a micro channel reactor at constant reformate feed inlet temperature of 350 °C. Coolant temperature ( ) 125 ( ) 200 ( ) 225 °C. Figure 2.46 Effect of coolant temperature on CO conversion for the water-gas shift reaction in a micro channel reactor at constant reformate feed inlet temperature of 350 °C. Coolant temperature ( ) 125 ( ) 200 ( ) 225 °C.
Extensive experimental determinations of overall heat transfer coefficients over packed reactor tubes suitable for selective oxidation are presented. The scope of the experiments covers the effects of tube diameter, coolant temperature, air mass velocity, packing size, shape and thermal conductivity. Various predictive models of heat transfer in packed beds are tested with the data. The best results (to within 10%) are obtained from a recently developed two-phase continuum model, incorporating combined conduction, convection and radiation, the latter being found to be significant under commercial operating conditions. [Pg.527]

Steady-state temperature Coolant temperature Feed flowrate Feed concentration Pre-exponential factor Heat transfer parameter (UAi Residence time Effective liquid volume... [Pg.94]

The behavior of gases dissolving in water appears to be less complex. The solubility of a gas in water typically decreases with increasing temperature, as shown for several cases in Fig. 17.6. This temperature effect has important environmental implications because of the widespread use of water from lakes and rivers for industrial cooling. After being used as a coolant, the water is returned to its natural source at a higher-than-ambient temperature (thermal pollution has occurred). Because it is warmer, this water contains less than the normal concentration of oxygen and is also less dense it... [Pg.837]

S. Brussovansky, J. Heywood and J. Keck, Predicting the Effects of Air and Coolant Temperature, Deposits, Spark Timing and Speed on Knock in Spark Ignition Engines, SAE Technical Paper 922324 (1992). [Pg.752]

We now have all the tools to solve reaction engineering problems involving heat effects in PFR for the cases of both constant and variable coolant temperatures. [Pg.502]

The temperature feedback mechanisms provide a link between the reactor s neutronics and its coolant systems independent of any action of the control system. The size and relative importance of the temperature effects will vary from reactor to reactor, but designers work hard to ensure that there is an overall negative coefficient of reactivity with temperature, which provides for automatic limiting or mitigation of temperature excursions. Some important temperature feedback mechanisms are listed below ... [Pg.280]

Uniform Surface Temperature, Foreign Gas as Coolant. The effectiveness of air injection in reducing convective heat flux stimulated investigations into the use of other coolants With the introduction of a foreign species into the boundary layer, the boundary layer equations reduce to the continuity equation (Eq. 6.6), the momentum equation (Eq. 6.7), the energy equation... [Pg.461]


See other pages where Coolant temperature, effect is mentioned: [Pg.349]    [Pg.404]    [Pg.559]    [Pg.106]    [Pg.331]    [Pg.33]    [Pg.48]    [Pg.190]    [Pg.1119]    [Pg.71]    [Pg.73]    [Pg.203]    [Pg.127]    [Pg.121]    [Pg.338]    [Pg.262]    [Pg.490]    [Pg.762]    [Pg.124]    [Pg.167]    [Pg.168]    [Pg.227]    [Pg.385]    [Pg.4]    [Pg.971]    [Pg.1456]    [Pg.1456]   
See also in sourсe #XX -- [ Pg.309 , Pg.310 ]




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Coolant temperature

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