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Air booster

Plug Forming Systems Warren Spring Labs, Takt-Shub (Buhler), Sturtevat External Air Injection Dynamic Air (Booster type system), Gericke (sonic nozzles) Internal Air By-pass - Fluidstat (Buhler), Turbuflow... [Pg.686]

The relative overall efficiency of the pumped LOX cycles vs. the LP cycle is a function of product pressure and the ef cienc y differences between the oxygen compressor and the air booster. Typically, the power consumption of both cycles is comparable. At higher pressures the pump work becomes more significant. The pumped LOX cycle is typically lower cost, due to the elimination of the oxygen compressor. [Pg.103]

The actuator system for a process control system in the CPI is typically composed of the control valve, the valve actuator, the I/P transmitter, and the instrument air system. The actuator system is known industrially as the final control element. In addition, a variety of optional equipment is designed to enhance the performance of the actuator system, such as valve stem positioners and instrument air boosters. [Pg.1187]

Process with Air Booster and Medium-Pressure Turbine for the Recovery of Compressed Oxygen, Nitrogen and Aigon... [Pg.21]

Table 2.5 Product spectrum of the process with air booster and medium pressure turbine (cf. also Fig. 2.3). Table 2.5 Product spectrum of the process with air booster and medium pressure turbine (cf. also Fig. 2.3).
I) Coldbox and battery limit for enthalpy balance (2) Filter (3) Main air compressor (4) Direct contact cooler (5) Evaporation cooler (6/6 ) Adsorber (7) Regeneration gas heater (8) Air booster (10) Heat exchanger ... [Pg.23]

FIGURE 35.8 Function of a heat-recovery unit with closed vapor hood (1, vapor hood 2, exhaust fan 3, supply air heat exchanger 4, supply air booster heater 5, fan for supply air 6, air distributor 7, pocket ventilation 8, room air heat exchanger 9, room air booster heater 10, temperature-control flaps 11, room-supply air fan 12, ceiling air distributor 13, air outlet louvers 14, warm-water unit 15, warm-water discharge). (Courtesy of J.M. Voith GmbH.)... [Pg.819]

Most gas-fired, heavy-duty gas turbines installed as of 1996 operate at gas pressures between 1.2 and 1.7 MPa (180—250 psig). However, aero derivative gas turbines and newer heavy-duty units can have such high air-inlet compression ratios as to require booster compressors to raise gas inlet pressures, in some cases as high as 5.2 MPa (750 psig). [Pg.17]

All of the benzoic acid producers in the United States employ the Hquid-phase toluene air oxidation process. As toluene becomes more important in the gasoline pool as an octane booster, the benzoic acid producers have to compete with gasoline marketers for the available toluene. If the attractiveness of toluene as an octane booster continues, the cost of producing benzoic acid will most likely increase. [Pg.54]

Figure 4-6. Ammonia combustion and absorption at air compressor discharge pressure of 3-12 bar (Process 2, elevated pressure), a = medium pressure, 3-6 bar b = high pressure, 6-12 bar, with interceding or booster compressor. Figure 4-6. Ammonia combustion and absorption at air compressor discharge pressure of 3-12 bar (Process 2, elevated pressure), a = medium pressure, 3-6 bar b = high pressure, 6-12 bar, with interceding or booster compressor.
The main purpose of pesticide formulation is to manufacture a product that has optimum biological efficiency, is convenient to use, and minimizes environmental impacts. The active ingredients are mixed with solvents, adjuvants (boosters), and fillers as necessary to achieve the desired formulation. The types of formulations include wettable powders, soluble concentrates, emulsion concentrates, oil-in-water emulsions, suspension concentrates, suspoemulsions, water-dispersible granules, dry granules, and controlled release, in which the active ingredient is released into the environment from a polymeric carrier, binder, absorbent, or encapsulant at a slow and effective rate. The formulation steps may generate air emissions, liquid effluents, and solid wastes. [Pg.70]

An evacuation booster or hogging ejector is sometimes used to remove air from a system on start-ups. Its capacity is set to bring the system pressure down to near operating conditions before the continuous operadng ejector system takes over. Figure 6-23 illustrates the instal-ladon of such a unit. [Pg.370]

Booster vacuum pumps are used to shorten the pump-down on evacuation (time) of a vacuum system before switching to the smaller vacuum pump to maintain the system opening vacuum and to handle the air inleakage to the system. [Pg.396]

In general, the number of boosters determines the operational flexibility of the unit with respect to the refrigeration load. A single booster unit operates continuously, regardless of load. A two booster unit can operate at 50% load by shutting off one unit at lower load levels it uses a pressure controller on the steam actuated by the condenser pressure. Because jets are not usually very flexible with respect to steam consumption and vacuum, load control may be in increments as compared to continuous variation. If a 100-ton unit is expected to operate an appreciable portion of the time at 25% of load, it may prove economical to install a four-booster unit and to operate only one for this period. Auxiliary ejectors remove uncondensed water vapor and air from the main condenser. [Pg.290]

In air drilling operation, large compressors and usually a booster compressor are used to compress atmospheric air and supply the required volumetric flowrate to the standpipe in much the same way that mud pumps supply mud for drilling. The volumetric flowrate of compressed air needed (which is usually stated in SCFM of air) depends upon the drilling rate, the geometry of the borehole to be drilled and the geometry of the drill string to be used to drill the hole [64,65]. [Pg.841]

The booster, which can compress air coming from the primary compressors to higher levels (i.e., on the order of 1,000 psig or higher), is always a piston-type compressor capable of variable volumetric flow and variable pressure output. [Pg.845]

Scrubber. This removes excess water from the injected air (or gas) stream to ensure that a minimum of moisture is circulated (if dry air for drilling is required) and to protect the booster. [Pg.846]

If the air volume used is too high, standpipe pressure will exceed the pressure rating of the compressor (and/or booster). Therefore, the compressor must be slowed down until air is mixed with the fluid going downhole. [Pg.848]

Installation arrangements, 351 Pump-down time, 380 Selection procedure, 374 Specification form, 377 Specifications, 373 Steam jet comparison, 356 Types of loads, 359 Ejectors, 346 Applications, 353 Barometric condenser, 249, 376 Booster, 370 Calculations Actual air capacity, 362 Air equivalent, 360... [Pg.626]

A trace air system uses a series of boosters employing a pressure regulator and a check valve. The Semco systems is depicted in Fig. 6. Dynamic Air incorporates a similar concept controlling the air volume rather than the pressure. [Pg.686]

Waeschle (Fig. 13) has developed a pressure sensing plug system. The boosters in this system are actuated by pressure rises in the line. The Fluid-Schub system of Buhler, Fig. 14, uses valves to inject air from an auxiliary air line. A system that produces extruded flow of long plugs can also be devised as shown in Fig. 15. [Pg.690]


See other pages where Air booster is mentioned: [Pg.102]    [Pg.109]    [Pg.779]    [Pg.49]    [Pg.102]    [Pg.109]    [Pg.779]    [Pg.49]    [Pg.23]    [Pg.49]    [Pg.127]    [Pg.327]    [Pg.327]    [Pg.1110]    [Pg.1942]    [Pg.447]    [Pg.399]    [Pg.276]    [Pg.159]    [Pg.420]    [Pg.642]    [Pg.841]    [Pg.844]    [Pg.1348]    [Pg.253]    [Pg.210]    [Pg.989]   
See also in sourсe #XX -- [ Pg.21 ]




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