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Figure C3.1.11. Apparatus for pump-probe time-resolved resonance Raman spectroscopy. (From Varotsis C and Babcock G T 1993 K4ethods Enzymol. 226 409-31.)... Figure C3.1.11. Apparatus for pump-probe time-resolved resonance Raman spectroscopy. (From Varotsis C and Babcock G T 1993 K4ethods Enzymol. 226 409-31.)...
Handling Temperatures. Optimum temperature for pumping is in 37—48°C range. Piping should be stainless steel, aluminum, or galvanized iron. Valves and pumps should be bronze, cast-iron with bronze trim, or stainless steel. A pump of 3.15-L/s (50-gal/min) capacity unloads a tank car of warm glycerol in ca 4 h. [Pg.349]

Other alloys have been developed for use in particular corrosive environments at high temperatures. Several of these are age-hardenable alloys which contain additions of aluminum and titanium. Eor example, INCONEL alloys 718 and X-750 [11145-80-5] (UNS N07750) have higher strength and better creep and stress mpture properties than alloy 600 and maintain the same good corrosion and oxidation resistance. AHoy 718 exhibits excellent stress mpture properties up to 705°C as well as good oxidation resistance up to 980°C and is widely used in gas turbines and other aerospace appHcations, and for pumps, nuclear reactor parts, and tooling. [Pg.7]

When petroleum occurs in a reservoir that allows the cmde material to be recovered by pumping operations as a free-flowing dark-to-light colored hquid, it is often referred to as conventional petroleum. In some oil fields, the downhole pressure is sufficient for recovery without the need for pumping. Heavy oil differs from conventional petroleum in that its flow properties are reduced and it is much more difficult to recover from the subsurface reservoir. These materials have a much higher viscosity and lower API (American Petroleum Institute) gravity than conventional petroleum, and primary recovery of these petroleum types usually requires thermal stimulation of the reservoir. [Pg.200]

Represents total pumped storage faciUty production minus energy used for pumping. [Pg.3]

If the pump manufacturer uses motors for pump power measurement, these motors ate caUbrated to determine the horsepower from the electric power reading and caUbration curves. Such test motors ate recaUbrated periodically, ensuring the same degree of accuracy as shown by the torque meters. [Pg.289]


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See also in sourсe #XX -- [ Pg.152 ]

See also in sourсe #XX -- [ Pg.152 ]




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Booster pump, use of, for hydrogenation

CO2 as a Working Fluid for Heat Pump Systems

Characteristic curves for centrifugal pumps

Compressed air for pumping

Detection Limit for Leakage Rates at Different Connection Positions of a Multistage Pumping System

Determine Pump Downtime for a System

Energy Requirements for Pumping

Example 3-16 Pump Performance Correction For Viscous Liquid

Example 6-14 Evacuation of Vessel Using Steam Jet for Pumping Gases

Flow inducer, pumps for liquids further reading

Flow inducer, pumps for liquids nomenclature

Flow inducer, pumps for liquids references

General operating information for vacuum pumps

Hydraulic Characteristics for Centrifugal Pumps

Impeller for chemical-handling pump

Infusion pump for

Mechanical Integrity Program for pumps

PUMPS FOR ROUGH AND HIGH VACUUM

Power requirements for pumping

Power requirements for pumping liquids

Pumping equipment for liquids

Pumps (Cont This page has been reformatted by knovel for easier navigation

Pumps (Cont equipment for

Pumps and compressors for supercritical extraction

Pumps applications for

Pumps casings for

Pumps for HPLC

Pumps for liquids

Pumps for recirculation

Pumps power requirements for

Pumps speeds for

Selection of pumps for drying processes

Some concluding comments on piping layout for pumps and compressors

Temperature Increase Calculation Example for a Screw Pump

Thermally Driven Hydrogel Actuator for Controllable Flow Rate Pump in Long-Term Drug Delivery

Transmittance for oil pumps

Traps for Pumps

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