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Control systems temperature

Temperature control systems incapable of handling multiple... [Pg.120]

Figure 2.2.4 (Berty 1983) shows a tubular reactor that has a thermosiphon temperature control system. The reaction is conducted in the vertical stainless steel tube that can have various diameters, 1/2 in. being the preferred size. If used for fixed bed catalytic studies, it can be charged with a single string of catalytic particles just a bit smaller than the tube, e.g., 5/16 particles in a l/2 O.D. tube. With a smaller catalyst, a tube with an inside diameter of up to three to four particle diameters can be used. With such catalyst charges and a reasonably high Reynolds number— above 500, based on particle diameter—this reactor... Figure 2.2.4 (Berty 1983) shows a tubular reactor that has a thermosiphon temperature control system. The reaction is conducted in the vertical stainless steel tube that can have various diameters, 1/2 in. being the preferred size. If used for fixed bed catalytic studies, it can be charged with a single string of catalytic particles just a bit smaller than the tube, e.g., 5/16 particles in a l/2 O.D. tube. With a smaller catalyst, a tube with an inside diameter of up to three to four particle diameters can be used. With such catalyst charges and a reasonably high Reynolds number— above 500, based on particle diameter—this reactor...
Examples of control systems Room temperature control system... [Pg.6]

Fig. 1.7 Block diagram of room temperature control system. Fig. 1.7 Block diagram of room temperature control system.
Example 4.6.2 Temperature control system (See also Appendix 1, examp462.m) The general form of a temperature control system is shown in Figure 1.6 with the corresponding block diagram given in Figure 1.7. [Pg.97]

Assuming that the temperature of the surroundings O it) remains constant, the closed-loop transfer function (using equation (4.130)) for the temperature control system, is... [Pg.99]

Fig. 4.34 Process reaction curve for the temperature control system shown in Figure 4.33. Fig. 4.34 Process reaction curve for the temperature control system shown in Figure 4.33.
Fig. 4.35 Closed-loop step response of temperature control system using PID controller tuned using Zeigler-Nichols process reaction method. Fig. 4.35 Closed-loop step response of temperature control system using PID controller tuned using Zeigler-Nichols process reaction method.
Excess temperature Temperature control system failure High inlet temperature High temperature... [Pg.402]

The electric heat tracer systems require good temperature control. A self-regulating system is shown in Figure 10-169. The manufacturers should he consulted to prepare proper temperature control systems. [Pg.244]

Burn-out can have only one meaning with a temperature-controlled system, and that is physical burn-out, which occurs when the surface temperature is made high enough to result in a rupture. Physical burn-out is a function of the mechanical properties of the surface material and of any load stresses it may carry. [Pg.211]

By maintaining the first-stage reactor just beyond the phase inversion point, the dispersed rubber phase is relatively rich in dissolved styrene. As polymerization subsequently proceeds in the LFR s, the dissolved styrene will react to form either a graft copolymer with the rubber or a homopolymer. The latter will remain within the rubber droplet as a separate occluded phase. Achieving the first-stage reactor conversion and temperature by recycling a portion of the hot second reactor effluent may permit simplification of the first reactor temperature control system. [Pg.106]

Suppose the reactor in Example 14.8 remains in batch mode after the fast-fill-and-hold startup. Will the temperature control system still work A preliminary answer based on the approximate kinetics of Example 14.7 is sufficient, but see the next problem. [Pg.536]

A first principle mathematical model of the extruder barrel and temperature control system was developed using time dependent partial differential equations in cylindrical coordinates in two spatial dimensions (r and z). There was no angular dependence in the temperature function (3T/30=O). The equation for this model is (from standard texts, i.e. 1-2) ... [Pg.493]

Figure 2.28. Simple feedback temperature control system. M-motor with stirrer, PV-pneumatic valve, Tx - temperature measurement, - temperature controller. Figure 2.28. Simple feedback temperature control system. M-motor with stirrer, PV-pneumatic valve, Tx - temperature measurement, - temperature controller.
Example 10.2 Consider the temperature control of a gas furnace used in heating a process stream. The probable disturbances are in the process stream temperature and flow rate, and the fuel gas flow rate. Draw the schematic diagram of the furnace temperature control system, and show how feedforward, feedback and cascade controls can all be implemented together to handle load changes. [Pg.197]

Figure 9 Lube Oil Cooler Temperature Control System and... Figure 9 Lube Oil Cooler Temperature Control System and...
Figure 9 shows a typical application of a block diagram to identify the operation of a temperature control system for lubricating oil. (A) in Figure 9 shows a schematic diagram of the lube oil cooler and its associated temperature control system. [Pg.118]

Only a few microwave reactors equipped with efficient temperature control systems for safe microwave synthesis at laboratory scale are currently available on the market. These systems lead to reproducible operating conditions. [Pg.23]

Ageing ovens are similar in nature to post-cure ovens requiring very accurate temperature control systems and monitoring for volume throughput of circulating air to ensure compliance with the requirements of specification testing. [Pg.199]

Are vaporizers provided with automatic gas line shutoff valve, downstream pressure-reducing valve, gas flow control valve, temperature control system and interlocks to shut down gas flow on low vaporizer temperature, and appropriate alarms in a continuously manned control room ... [Pg.84]

The dominant pole of this temperature control system is also determined by the thermal time constant of the microhotplate, which is approximately 20 ms. The open-loop gain of the differential analog architecture (Aql daa) is given by Eq. (5.8) ... [Pg.80]

Most ultrasonic experiments are carried out in temperature controlled systems to ensure that isothermal conditions are maintained. Even a small general increase in microbial temperature can influence both the active and passive transport systems of the cell membrane/wall and this in turn may lead to an increased uptake of compounds. If the temperature is not controlled then sonication could result in a large temperature increase which will lead to the denaturation (deactivation) of enzymes, proteins and other cellular components present within the microorganism [7]. [Pg.133]


See other pages where Control systems temperature is mentioned: [Pg.6]    [Pg.98]    [Pg.879]    [Pg.1257]    [Pg.300]    [Pg.13]    [Pg.207]    [Pg.210]    [Pg.212]    [Pg.409]    [Pg.819]    [Pg.490]    [Pg.490]    [Pg.537]    [Pg.78]    [Pg.102]    [Pg.132]    [Pg.21]    [Pg.168]    [Pg.5]    [Pg.11]    [Pg.17]   
See also in sourсe #XX -- [ Pg.278 ]

See also in sourсe #XX -- [ Pg.97 ]

See also in sourсe #XX -- [ Pg.169 , Pg.204 , Pg.233 ]

See also in sourсe #XX -- [ Pg.116 ]




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