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Vortex tube, heated

Cap the tubes, vortex, and heat 35 min in a boiling water bath. [Pg.549]

A vortex tube has certain advantages as a chemical reactor, especially if the reactions are endothermic, the reaction pathways are temperature dependent, and the products are temperature sensitive. With low temperature differences, the vortex reactor can transmit enormous heat fluxes to a process stream containing entrained solids. This reactor is ideally suited for the production of pyrolysis oils from biomass at low pressures and residence times to produce about 10 wt % char, 13% water, 7% gas, and 70% oxygenated primary oil vapors based on mass balances. This product distribution was verified by carbon, hydrogen, and oxygen elemental balances. The oil production appears to form by fragmenting all of the major constituents of the biomass. [Pg.31]

EPON. Put 20.0 g EPON, 13.0 g Dodecenyl succinic anhydride (DDSA) and 11.5 g Methyl nadic anhydride (MNA) into the same test-tube. Heat the tube in the oven for 2-3 min at 60° and then vortex it well. Add 0.9 g tri-Dimethylaminomethyl phenol (DMP-30, all from Electron Microscopy Sciences, Fort Washington, PA) and immediately vortex the tube again. It is possible to freeze the EPON in aliquots and to store it for a long time at -20° before use. [Pg.49]

Fig. 23-2. Two examples of traps. A shows a trap packed with Porapak N cooled to -15 °C with air from a Vortex tube and heated during desorption by an electrical current through the trap. B shows an open tubular trap cooled in the vapours of liquid nitrogen. The trap is heated for desorption of the halocar-bons either by immersing it into boiling hot water or by an electrical current through the tube. See text for details. Fig. 23-2. Two examples of traps. A shows a trap packed with Porapak N cooled to -15 °C with air from a Vortex tube and heated during desorption by an electrical current through the trap. B shows an open tubular trap cooled in the vapours of liquid nitrogen. The trap is heated for desorption of the halocar-bons either by immersing it into boiling hot water or by an electrical current through the tube. See text for details.
Vortex tubes run on compressed air and. with adjusmient. can produce either cool air or warm air. Operations requiring heavy protective clothing build up the wearer s body temperature. Some workers tire from heat stress or the inability of the body to remove the heat buildup due to physical activity, lack of ventilation, radiation or all three. The standard suit provides cooling for up to 200 F, but specialty suits and different styles are sold by various manufacturers. [Pg.95]

The foil suit system is well designed for use up to 200 F. In selecting the proper man cooling equipment, the source of heat is as important as the amount. Whenever the heat is primarily radiant, a reflectorized system is indicated. For example, workers near furnaces, forging presses, ovens, etc., should use the reflectorized clothing. The reflective coating will reflect up to 90% of incident radiant heat. Of course, any heat reflected does not have to be ofl%t by the vortex tube air conditioner. Systems are not intended to be used in severe heat situations, such as oven entry and tire entry applications. Highly specialized, very expensive equipment is made for these applications. [Pg.96]

Sample preparation Vortex 200 iL plasma with 50 pL 20% trichloroacetic acid in water, centrifuge at 1300 g for 15 min. Remove 150 pL of the supernatant and mix it with 50 pL 160 mM chloroacetaldehyde in water containing 2 M sodium acetate, vortex, close the tube, heat at 98° for 30 min, cool to 2°, vortex, inject a 20 pL aliquot. [Pg.11]

Some chemical fume hoods have compressed air lines that allow the use of air operated equipment such as vortex tubes (for heating and cooling). When using vortex tubes inside a fume hood, the sash should be fuUy closed because additional air flow inside the hood is present. [Pg.2529]

The fourth step was the pursuit of an investigation of auxiliary cooling. All known methods of reducing heat stress applicable to this concept were reviewed from the Vortex tube to the Peltier effect. Hardware tested and rejected included ... [Pg.198]

High Temperature. The low coefficient of thermal expansion and high thermal conductivity of sihcon carbide bestow it with excellent thermal shock resistance. Combined with its outstanding corrosion resistance, it is used in heat-transfer components such as recuperator tubes, and furnace components such as thermocouple protection tubes, cmcibles, and burner components. Sihcon carbide is being used for prototype automotive gas turbine engine components such as transition ducts, combustor baffles, and pilot combustor support (145). It is also being used in the fabrication of rotors, vanes, vortex, and combustor. [Pg.468]

In a submerged-tube FC evaporator, all heat is imparted as sensible heat, resulting in a temperature rise of the circulating hquor that reduces the overall temperature difference available for heat transfer. Temperature rise, tube proportions, tube velocity, and head requirements on the circulating pump all influence the selec tion of circulation rate. Head requirements are frequently difficult to estimate since they consist not only of the usual friction, entrance and contraction, and elevation losses when the return to the flash chamber is above the liquid level but also of increased friction losses due to flashing in the return line and vortex losses in the flash chamber. Circulation is sometimes limited by vapor in the pump suction hne. This may be drawn in as a result of inadequate vapor-liquid separation or may come from vortices near the pump suction connection to the body or may be formed in the line itself by short circuiting from heater outlet to pump inlet of liquor that has not flashed completely to equilibrium at the pressure in the vapor head. [Pg.1139]

A vertical cylindrical, and mechanical agitated pressure vessel, equipped with baffles to prevent vortex formation is the most widely used fermenter configuration. The baffles are typically one-tenth of the fermenter diameter in widtli, and are welded to supports tliat extend from the sidewall. A small space between the sidewall and the baffle enables cleaning. Internal heat transfer tube bundles can also be used as baffles. The vessels must withstand a 45 psig internal pressure and full vacuum of -14.7 psig, and comply with the ASME code. [Pg.857]

Finally, we come to the effects of the Lewis number. Figure 4.2.14 shows the intensified images of vortex ring combustion of lean and rich propane/air mixtures. Since the flame is curved and stretched at the head region, the mass and heat is transferred through a stream tube. [Pg.54]


See other pages where Vortex tube, heated is mentioned: [Pg.472]    [Pg.26]    [Pg.360]    [Pg.472]    [Pg.93]    [Pg.26]    [Pg.139]    [Pg.140]    [Pg.143]    [Pg.252]    [Pg.307]    [Pg.135]    [Pg.677]    [Pg.753]    [Pg.33]    [Pg.472]    [Pg.117]    [Pg.34]    [Pg.34]    [Pg.37]    [Pg.37]    [Pg.753]    [Pg.753]    [Pg.510]    [Pg.511]    [Pg.352]    [Pg.115]    [Pg.668]    [Pg.670]    [Pg.55]    [Pg.152]    [Pg.1159]    [Pg.938]    [Pg.285]   
See also in sourсe #XX -- [ Pg.140 ]




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