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Gauges axial

The finite element model described in Section 11.2 was used here to model the friction experiments described above. However, to simulate the 16 Nm torque, a bolt pre-stress of 227 MPa was applied. This value was obtained experimentally from the axial gauges in the shank of a specially manufactured instmmented bolt, as discussed previously. For comparison, both the continuous and stick-slip [25] fiiction models (available in MSC Marc finite element code) was used to account for fiiction between the contacting interfaces. The fiiction coefficients were chosen to be 0.1, 0.3 and 0.45 between the bolt/laminate, washer/laminate and laminate/laminate interfaces, respectively. More details on fiiction coefficient selection can be found in [17]. [Pg.305]

Note that in the above axial gauges the propagator is orthogonal to n and is orthogonal to when k = 0. [Pg.453]

An alternate method not used too much at this time is the drum design. The drum construction is somewhat different from the disc, in that the rotor body is of cylindrical construction. By using the hollow drum, conical roots, of bolted construction, can be used for the rotor, again, allowing for stagger adjustments to fine tune the axial compressor to the application if the need arises. The setting is done to a gauge at the factory, as with the stators. [Pg.249]

In order to check the gauging method, applied here, by axial-anomaly low-energy theorem, GG —> 2 photons correlator (M.M. Musakhanov et.al., 2003) was calculated. It was found that this gauged QCD low-energy effective action perfectly satisfies the theorem (M.M. Musakhanov et.al., 2003). [Pg.267]

Tab. 8.3 Axial properties of CNT fibers at long gauge lengths, ideal graphene layer and other materials. Tab. 8.3 Axial properties of CNT fibers at long gauge lengths, ideal graphene layer and other materials.
Early design and simulation of large-diameter, melt-fed extruders were described by Fenner [17]. A numerical simulation of the axial pressure and temperature fora screw similar to that shown in Fig. 15.8 is shown in Fig. 15.10. This simulation was performed using a three-dimensional method using a finite difference approach. The process starts with an LDPE resin (2 dg/min, 2.16 kg, 190 °C) in the low-pressure separator at a pressure of 0.04 MPa (gauge) and a temperature of 230 °C. [Pg.666]

The mass of the chiral 1,2 -bosons will then vanish, while the mass of the chiral 3-boson will be m. So rather than strictly setting A3 = 0, it is a separate chiral gauge field that obeys axial vector nonconservation and only occurs at short ranges. [Pg.416]

Fig. 10.50 Location of the pressure gauge (P) and the thermocouples (7) at the five axial barrel positions. The three cross sections A-A, B-B and C-C are used for contour plots of the numerical results. [Reprinted by permission from T. Ishikawa, S. Kihara, K. Funatsu, T. Amaiwa, and K. Yano, Numerical Simulation and Experimental Verification of Nonisothermal Flow in Counterrotating Nonintermeshing Continuous Mixers, Polym. Eng. Sci., 40, 365 (2000).]... Fig. 10.50 Location of the pressure gauge (P) and the thermocouples (7) at the five axial barrel positions. The three cross sections A-A, B-B and C-C are used for contour plots of the numerical results. [Reprinted by permission from T. Ishikawa, S. Kihara, K. Funatsu, T. Amaiwa, and K. Yano, Numerical Simulation and Experimental Verification of Nonisothermal Flow in Counterrotating Nonintermeshing Continuous Mixers, Polym. Eng. Sci., 40, 365 (2000).]...
Thermal Conductivity Vacuum Gauges. A very widely applied gauge of this type is the Pirani gauge. Such gauges consist of a wire (Pt, W or Ni, d = 5-20 pm / 5 cm) mounted axially in a cylindrical tube (d 2 cm). The wire is heated by an electric current to approximately 100°C above the ambient temperature and heat loss occurs by three mechanisms, as indicated in Figure 5.3. [Pg.152]

The experimental system used in this study is shown in Figure 1. The trickle-bed reactor was made up of 1.27-cm (Vi-in) OD, Type 316 stainless steel tubing with 0.32-cm (Vi-in.) OD, centrally located thermowell tubing. The reactor was packed with 8/10 mesh catalyst particles. The nominal reactor temperature was measured by a thermocouple which could traverse axially along the thermowell from the top to the bottom of the catalyst bed. The nominal reactor pressure was measured by a Heise gauge which was located upstream from the reactor. [Pg.180]

Mechanical properties of the composite materials were tested by a hydraulic-driven MTS tensile tester manufactured by MTS Systems Corporation, Minneapolis, Minnesota. A strain-rate of 5x 10 5 s 1 was used. During deformation, the linear actuactor position was monitored and controlled by a linear variable differential transformer (LVDT), while strain was measured using MTS-brand axial and diametral strain-gauge extensometers. The axial extensometer serves to measure the tensile deformation in the direction of loading while the diametral extensometer serves to measure the compressive deformation at 90° to the loading axis due to Poisson s contraction. All tensile tests were performed at 23 °C and in accordance to ASTM D3518-76. [Pg.129]


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See also in sourсe #XX -- [ Pg.2 , Pg.114 ]




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