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Process load

The bowl is suspended from an upper bearing and drive (electric or turbine motor) assembly through a flexible-drive spindle with a loose guide in a controlled damping assembly at the bottom. The unit finds its axis of rotation if it becomes slightly unbalanced due to process load. [Pg.1730]

Historically, the most popular driver for the centrifugal compressor has been the steam turbine. Steam turbines can readily be speed matched to the compressor. Prior to the upsurge in energy costs, reliability, simplicity, and operational convenience were the primary factors in driver selection. The steam turbine, with its ability to operate over a relatively wide speed range, was ideal for the centrifugal compressor, which could be matched to the process load by speed modulation. [Pg.146]

In case use of local protection system effect on exposure of the process, load calculations shall he revised. products... [Pg.18]

Internal heating load Heat gains that occur in a space from process loads, lighting, solar gain, occupants, machines, etc. [Pg.1452]

Figure 6-32 illustrates ejector systems with large condensable loads which can be at least partially handled in the precondenser. Controls are used to maintain constant suction pressure at varying loads (air bleed), or to reduce the required cooling water at low process loads or low water temperatures [2]. The cooler W ater must not be throttled below the minimum (usually 30%-50% of maximum) for proper contact in the condenser. It may be controlled by tailwater temperature, or by the absolute pressure. [Pg.379]

In many processes, load recuperation is not practicable, and combustion air is preheated in a heat exchanger by means of the outgoing flue products. Figure 19.3 gives an indication of the savings to be made for different operating temperatures. It is not normally considered economic to operate a recuperator at flue temperatures below about 750°C. [Pg.266]

Moving now to two boilers, the heat load may comprise two elements. One may be a production process whose interruption would cause problems and the other, say, a heating load where any interruption would not be noticed immediately. Assuming the two elements were of equal duty, it would be reasonable to install two boilers each 50-50 per cent of the total load. One boiler would then be able to cover the process load. [Pg.354]

The reason for speed variations in constant-speed machinery is variation of process load. For example, a centrifugal pump s load will vary due to the viscosity of the fluid being pumped or changes in suction or discharge pressure. The pump speed will change because of these load changes. [Pg.714]

An imbalance profile can be excited due to the combined factors of mechanical imbalance, lift/gravity differential effects, aerodynamic and hydraulic instabilities, process loading, and, in fact, all failure modes. [Pg.734]

Substrate to micro-organism ratio or process load factor... [Pg.578]

Figure 11.11 gives the IMC structure. The model of the process is run in parallel with the actual process. The output of the model is subtracted from the actual output of the process X and this signal is fed hack into the controller. This signal is, in a sense, the effect of load disturbances on the output (since we have subtracted the effect of the manipulated variable M). Thus we are inferring the load disturbance without having to measure it. This signal is Xi, the output of the process load transfer function, and is equal to We... [Pg.404]

Figure 8.24. Simpler circuits of compression refrigeration (see also Example 8.17). (a) Basic circuit consisting of a compressor, condenser, expansion valve and evaporator (load), (b) Conditions of the basic circuit as they appear on a pressure-enthalpy diagram the primed points are on the vapor-liquid boundary curve, (c) Circuit with circulation of refrigerated brine to process loads, (d) Circuit with two-stage compression and intercooling. Figure 8.24. Simpler circuits of compression refrigeration (see also Example 8.17). (a) Basic circuit consisting of a compressor, condenser, expansion valve and evaporator (load), (b) Conditions of the basic circuit as they appear on a pressure-enthalpy diagram the primed points are on the vapor-liquid boundary curve, (c) Circuit with circulation of refrigerated brine to process loads, (d) Circuit with two-stage compression and intercooling.
So what value, if any, do physical measurements have with respect to the validation of sterilization processes Their primary utility is in the comparison of one process to another. This can be done in myriad ways (process to process, load to load, item to item, etc.), and forms the basis for claims of uniformity and reproducibility for the process. [Pg.104]

Tube-axial fans are provided with adjustable pitch blades that permit the balancing of the fan to match the varying process load either automatically or by infrequent manual adjustments. Vane-axial fans are also available with controllable pitch blades (that is, pitch that can be varied while the fan is in operation) for use when frequent or continuous flow adjustment is needed. [Pg.260]

At the level flow, there is a load and hence a load conductance corresponding to the state of optimal efficiency between the static head and the level flow. The dissipation of oxidative phosphorylation with a coupled process (load) utilizing ATP is given as follows... [Pg.570]

Water batching combines multiple systems (process and utility) to simulate production conditions using water or process materials, if necessary. Water batching may be done in combination with other OQ tests. Wet loop checking and water batching often use water to simulate process loads but, if necessary, may use actual process materials. [Pg.632]


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