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Level temperature profile

The simple checks need to be made first. These include column liquid level, temperature profile, pressure profile and stream flow rates. In addition, a Delta-P. survey using test gauges should be made in the field and if not by the troubleshooter then under his direct supervision. Just... [Pg.297]

Modern regenerator-burner packages permit low-end exit gas temperatures (400 to 500 F or 205 to 260 C) at every regenerator-burner an)wvhere in the furnace, and for process temperatures as high as 2500 F (1370 C), the high-productivity level temperature profile can be as efiflcient as a graduated temperature profile. [Pg.119]

AlO. Conventionally, excess air has been used to reduce temperature differences along the gas flow paths, but that approach costs more fuel. With pulsed flows, high mass flows accomplish the same more-level temperature profile as excess air but without the fuel cost and without the necessary added soak time. Stepped pulse firing allows soak times between its pulses. [Pg.241]

Comparisons of the complete heat-transfer model with pilot-scale rotary kiln data are shown iu Figure 5 (21) for moisture levels ranging from 0 to 20 wt %. The tremendous thermal impact of moisture is clearly visible iu the leveling of temperature profiles at 100°C. [Pg.50]

The other method is the prescribed velocity (PV) method. In this method only the streamwise velocity component U and the temperature profile are prescribed inside the volume ab. The remaining variables ( V, W, k, and e) are solved for as usual in the whole room, including the ab volume. The temperature level has to be readjusted after each iteration to ensure conservation of energy. [Pg.1043]

Figure 12.41 shows the results of three experiments with a similar Archimedes number and different Reynolds numbers. The figure shows vertical temperature profiles in a room ventilated by displacement ventilation. The dimensionless profiles are similar within the flow rates shown in the figure, although the profile may involve areas with a low turbulence level in the middle of the room. A test of this type could indicate that further experiments can be performed independently of the Reynolds numbers. [Pg.1193]

When the emulsification was complete, the gear pump speed was reduced to the desired level and the flow rates of the emulsion and of the initiator were established. Temperature profiles and pressure drops along the reactor were recorded and the flow rate was measured gravimetrically. [Pg.118]

As far as extinction/ignition behavior is concerned, oxidations in micro reactors can exhibit varied temperature profiles [19, 56, 57, 59-61]. As a consequence of their very distinct heat transfer characteristics, micro reactors can allow autofhermal operation at a different temperature level compared with processing in conventional reactors. As an example, this may raise the selectivity of value products. [Pg.292]

It should be emphasized that for ideal tubular reactors, it is the total volume per unit of feed that determines the conversion level achieved. The ratio of the length of the tube to its diameter is irrelevant, provided that plug flow is maintained and that one uses the same flow rates and pressure-temperature profiles expressed in terms of reactor volume elements. [Pg.264]

Here, one may employ a higher temperature for the second-stage feed and still achieve the desired conversion level. The conversion and temperature profiles as calculated from equations A and B are given in Table 12.1.2. [Pg.518]

Fig. 2.7 Temperature profiles for a 30mL sample of 1-methyl-2-pyrrolidone heated under open-vessel microwave irradiation conditions [19]. Multimode microwave heating at different maximum power levels for 6 min with temperature control using the feedback from a fiber-... Fig. 2.7 Temperature profiles for a 30mL sample of 1-methyl-2-pyrrolidone heated under open-vessel microwave irradiation conditions [19]. Multimode microwave heating at different maximum power levels for 6 min with temperature control using the feedback from a fiber-...
Level (3) global e.g., reactor model some key parameters reactor volume, mixing/flow, residence time distribution, temperature profile, reactor type... [Pg.3]


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Temperature level

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