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Containment external pressure loads

In production the filled container—with the lid loosely applied—is fed into a vacuum chamber where a vacuum is first applied followed by a top loading to force the lid into intimate contact with the container rim. When the external pressure is restored to atmospheric, the vacuum within the container maintains the seal. The effectiveness of the closure can be checked visually or automatically by observing a depression in the lid due to the pressure differential. The container is opened by releasing the vacuum with the aid of a coin slot built into the base. Both container and lid are constructed of tinplate rather than aluminium and in a fairly thick gauge in order to withstand the pressures applied. [Pg.293]

The instrumentation of HPCE is uncomplicated (see the schematic drawing in Figure 1). Briefly, both ends of the narrow-bore fused silica capillary are immersed into reservoirs containing a buffer solution that also fills the capillary. The reservoirs also contain electrodes that provide electrical contact between the high-voltage power supply and the capillary. The sample is loaded onto the capillary by replacing one of the buffer reservoirs by a sample reservoir and applying external pressure (hydrodynamic injection) or an electric field (electrokinetic injection). After the injection, the reservoir is replaced, the electrical field is applied, and the separation starts. The detection is usually performed at the opposite end of the capillary (normal polarity mode). UV/vis detection is by far the most common detection technique in HPCE. Other techniques include fluorescence, amperometry, conductivity, and mass spectrometry. Modem HPCE instruments are fully automated and thereby allow easy operations and precise quantitative analyses. [Pg.542]

Major loads that induce compressive stresses in the containment vessel are internal and external pressure and crane and seismic loads. [Pg.298]

Another rapid loading condition in underwater applications is the application of external hydrostatic stress to plastic structures (also steel, etc.). Internal pressure applications such as those encountered in pipe and tubing or in pressure vessels such as aerosol containers are easily treated using tensile stress and creep properties of the plastic with the appropriate relationships for hoop and membrane stresses. The application of external pressure, especially high static pressure, has a rather unique effect on plastics. The stress analysis for thick walled spherical and tubular structures under external pressure is available. [Pg.110]

The state vector Zn o contains four elements of which two are known from the boundary conditions prescribed at station 0. The other two elements in the state vector can be estimated from equation (34) by applying appropriate conditions at the extreme ends of the stiffened panel array. To include the effect of random pressure and external point loads acting on the skin stringer panel, equation (34) can be modified by adding the load transfer matrix [ En o from equation (26). [Pg.462]

A tall, vertically supported vessel which is subjected to external pressure and external loading contains stresses similar to fliose in a vessel with external pressure only. The method of combining loadings as developed by Bergman and described in Section I6.S is used to obtain used in the analysis. [Pg.660]

Fig. 9.6. Schematic representation of die BEST system (Brnker Biospin see also [21]). 1, Bottle with transport liquid 2, dilutor 402 single syringe (5mL) with 1100 iL tube 3, dilutor 402 3-way valve 4, sample loop (250-500 pL) 5, 6-way valve (standard version) loading sample 6, 6-way valve (standard version) injecting sample 7, injection port 8, XYZ needle 9, rack for sample vials 10, rack for recovering vials 11, rack for washing fluids and waste bottle (3 glass bottles) 12, external waste bottle 13, flow probe with inner lock container 14, inert gas pressure canister for drying process. Fig. 9.6. Schematic representation of die BEST system (Brnker Biospin see also [21]). 1, Bottle with transport liquid 2, dilutor 402 single syringe (5mL) with 1100 iL tube 3, dilutor 402 3-way valve 4, sample loop (250-500 pL) 5, 6-way valve (standard version) loading sample 6, 6-way valve (standard version) injecting sample 7, injection port 8, XYZ needle 9, rack for sample vials 10, rack for recovering vials 11, rack for washing fluids and waste bottle (3 glass bottles) 12, external waste bottle 13, flow probe with inner lock container 14, inert gas pressure canister for drying process.
Using this instrument in Figure 6.5, Handa (1986b) measured the heat input to a hydrate sample in the sample container S, relative to helium at ambient temperature and 5 kPa in reference cell R. The hydrate was externally prepared from ice in a rolling-rod mill, before a 4 g sample was loaded into the calorimeter at liquid nitrogen temperatures. For heat capacity measurements, a pressure greater than the hydrate dissociation pressure was maintained in the sample cell. By cycling... [Pg.340]

Let us first restrict to the simpler and more frequently encountered case that the feed mixture consists of vapors of a single component B in the carrier gas A. The optimum device, both at ambient and elevated pressure, will then be a saturator which contains component B in the solid or liquid state (Fig. 2). On its way through the saturator, the carrier gas A is loaded with vapors of B. Since its vapor pressure depends exponentially on the temperature, the saturator must be thoroughly thermostated. An externally thermostated water or oil bath circulating through a jacket around the saturator is often the best solution. If temperatures above ca. 200 °C are required, a saturator surrounded by a stirred bath of molten salt with an efficient temperature control can be used alternatively. [Pg.403]

Figure 6.11. Nyquist plots for MEAs containing different proton-conducting ionomers at 0.85 V without external humidification catalyst loading = 0.4, 0.7 mg Pt/cm2 for anode and cathode, respectively TceU = 25°C Pressure = 1 atm and H2/02 flow = 400 cmVmin [8]. (Reprinted from Electrochimica Acta, 50(2-3), Ahn SY, Lee YC, Ha HY, Hong SA, Oh IH. Effect of the ionomers in the electrode on the performance of PEMFC under non-humidifying conditions, 673-6, 2004, with permission from Elsevier.)... Figure 6.11. Nyquist plots for MEAs containing different proton-conducting ionomers at 0.85 V without external humidification catalyst loading = 0.4, 0.7 mg Pt/cm2 for anode and cathode, respectively TceU = 25°C Pressure = 1 atm and H2/02 flow = 400 cmVmin [8]. (Reprinted from Electrochimica Acta, 50(2-3), Ahn SY, Lee YC, Ha HY, Hong SA, Oh IH. Effect of the ionomers in the electrode on the performance of PEMFC under non-humidifying conditions, 673-6, 2004, with permission from Elsevier.)...
For more thorough flash removal, moderately abrasive material is added to the tumbling method described above. This media deflashing allows both internal and external flash to be removed. The parts to be deflashed are loaded into a container. Once the tumbling starts an abrasive media material (ground walnuts, hard nylon, polycarbonate pellets, etc.) is directed at the parts under air pressure and... [Pg.128]


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See also in sourсe #XX -- [ Pg.51 ]




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