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Friction tubes

Friction Igniters or Primers (Also known as Friction Tubes). They are devices for the production of fire by the friction of the thnist, gjtVi or push, or pu 11, of a roughened rod or wire... [Pg.585]

Since the tube friction factor measures the force needed to impart a unit velocity to the chain along the tube direction, we can think of applying this force, one segment at a time, to the diffusing chain. Since the friction factor per segment is f, Eq. (2.65) becomes... [Pg.122]

Fig. 2. Friction factors for cylindrical pipe where line A represents drawn tubing line B, commercial steel C, galvanised iron and lines D, E, and F,... Fig. 2. Friction factors for cylindrical pipe where line A represents drawn tubing line B, commercial steel C, galvanised iron and lines D, E, and F,...
Further reductions in reservoir pressure move the shock front downstream until it reaches the outlet of the no22le E. If the reservoir pressure is reduced further, the shock front is displaced to the end of the tube, and is replaced by an obflque shock, F, no pressure change, G, or an expansion fan, H, at the tube exit. Flow is now thermodynamically reversible all the way to the tube exit and is supersonic in the tube. In practice, frictional losses limit the length of the tube in which supersonic flow can be obtained to no more than 100 pipe diameters. [Pg.95]

Friction due to lack of vertical positioning of the tube is a source of error, as is sensitivity to the surface condition of the test piece. Samples of small mass cannot be tested except when supported on a heavy anvil. [Pg.467]

Friction Coefficient. In the design of a heat exchanger, the pumping requirement is an important consideration. For a fully developed laminar flow, the pressure drop inside a tube is inversely proportional to the fourth power of the inside tube diameter. For a turbulent flow, the pressure drop is inversely proportional to D where n Hes between 4.8 and 5. In general, the internal tube diameter, plays the most important role in the deterrnination of the pumping requirement. It can be calculated using the Darcy friction coefficient,, defined as... [Pg.483]

Correlations for Convective Heat Transfer. In the design or sizing of a heat exchanger, the heat-transfer coefficients on the inner and outer walls of the tube and the friction coefficient in the tube must be calculated. Summaries of the various correlations for convective heat-transfer coefficients for internal and external flows are given in Tables 3 and 4, respectively, in terms of the Nusselt number. In addition, the friction coefficient is given for the deterrnination of the pumping requirement. [Pg.483]

Table 3. Correlations for Convective Heat-Transfer and Friction Coefficients for Circular Tube Flow ... Table 3. Correlations for Convective Heat-Transfer and Friction Coefficients for Circular Tube Flow ...
SheUside flow maldistribution effect is normally iacluded in the, -correction. Tubeside flow maldistribution effect is relatively small in most designs because the principal resistances are tube friction and entrance/exit pressure drop. [Pg.489]

Frictiona.1 Pressure Drop. The frictional pressure drop inside a heat exchanger results when fluid particles move at different velocities because of the presence of stmctural walls such as tubes, shell, channels, etc. It is calculated from a weU-known expression of... [Pg.490]

The fluid dehvery in an air-spray system can be pressure or suction fed. In a pressure-fed system, the fluid is brought to the atomizer under positive pressure generated with an external pump, a gas pressure over the coating material in a tank, or an elevation head. In a suction system, the annular flow of air around the fluid tip generates sufficient vacuum to aspirate the coating material from a container through a fluid tube and into the air stream. In this case, the paint supply is normally located in a small cup attached to the spray device to keep the elevation differential and frictional pressure drop in the fluid-supply tube small. [Pg.330]

Fanning friction factor /i for inner wall and / 2 for outer wall of annulus /l for ideal tube bank sldn friction drag coefficient Dimensionless Dimensionless... [Pg.549]

Rothfus, Monrad, Sikchi, and Heideger [Ind. Eng. Chem., 47, 913 (1955)] report that the friction factor/g for the outer wall bears the same relation to the Reynolds number for the outer portion of the anniilar stream 2(r9 — A, )Vp/r9 l as the fricBon factor for circular tubes does to the Reynolds number for circular tubes, where / is the radius of the outer tube and is the position of maximum velocity in... [Pg.563]

For turbulent flow in smooth tubes, the Blasius equation gives the friction facdor accurately for a wide range of Reynolds numbers. [Pg.636]

In laminar flow,/is independent of /D. In turbulent flow, the friction factor for rough pipe follows the smooth tube curve for a range of Reynolds numbers (hydrauhcaUy smooth flow). For greater Reynolds numbers,/deviates from the smooth pipe cui ve, eventually becoming independent of Re. This region, often called complete turbulence, is frequently encountered in commercial pipe flows. The Reynolds number above which / becomes essentially independent of Re is (Davies, Turbulence Phenomena, Academic, New York, 1972, p. 37) 20[3.2-2.46ln( /D) ... [Pg.637]


See other pages where Friction tubes is mentioned: [Pg.196]    [Pg.25]    [Pg.453]    [Pg.474]    [Pg.196]    [Pg.25]    [Pg.453]    [Pg.474]    [Pg.225]    [Pg.39]    [Pg.114]    [Pg.122]    [Pg.344]    [Pg.297]    [Pg.353]    [Pg.466]    [Pg.490]    [Pg.491]    [Pg.492]    [Pg.211]    [Pg.78]    [Pg.562]    [Pg.124]    [Pg.7]    [Pg.349]    [Pg.512]    [Pg.578]    [Pg.91]    [Pg.472]    [Pg.474]    [Pg.474]    [Pg.477]    [Pg.477]    [Pg.625]    [Pg.638]    [Pg.662]   
See also in sourсe #XX -- [ Pg.453 ]

See also in sourсe #XX -- [ Pg.453 ]




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