2010
DOI: 10.1016/j.apm.2009.10.014
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Turbulent flow around single concentric long capsule in a pipe

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Cited by 20 publications
(21 citation statements)
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“…In the results measured by Liu and Graze, [28] the place where the variation of pressure is great is also the location of the coal log. When they measured the pressure, the coal log was fixed on the pipe, similar to the case of t ¼ 0.01 s. Figure 9 compares the pressure distribution at the coal log surface over time with the pressure measured by Liu and Graze [28] and the simulation data of Khalil et al [3] The operating conditions of their studies are listed in Table 3. At t ¼ 0.01 s, the pressure at the upstream end of the coal log is nearly equal to the pressure of the inlet.…”
Section: Model Validationmentioning
confidence: 98%
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“…In the results measured by Liu and Graze, [28] the place where the variation of pressure is great is also the location of the coal log. When they measured the pressure, the coal log was fixed on the pipe, similar to the case of t ¼ 0.01 s. Figure 9 compares the pressure distribution at the coal log surface over time with the pressure measured by Liu and Graze [28] and the simulation data of Khalil et al [3] The operating conditions of their studies are listed in Table 3. At t ¼ 0.01 s, the pressure at the upstream end of the coal log is nearly equal to the pressure of the inlet.…”
Section: Model Validationmentioning
confidence: 98%
“…[10] Khalil et al built a dynamic model of turbulent flow around a single long capsule situated in a concentric position using the commercial software FLUENT 6.3 by directly setting the capsule velocity. [3] Based on Fluent, Asim et al also obtained a numerical solution governing the turbulent flow around a concentric cylindrical capsule. [11] The geometries of the capsule models and pipes of these studies are listed in Table 1.…”
Section: Literature Reviewmentioning
confidence: 98%
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“…A practical range of inlet flow velocities have been considered here, corresponding to a 100mm diameter pipeline, as considered by many other researchers [9,[18][19][20][21][22][26][27][28]. All the walls in the flow domain have been modelled using no-slip boundary condition, as is expected in real world scenarios [38][39].…”
Section: Boundary Conditionsmentioning
confidence: 99%
“…These pressure drops have already been defined in equation (5)(6)(7)(8)(9), were λ w can be found by the Moody's approximation as [52]: (26) and Ω w has been found out to be:…”
Section: Total Pressure Dropmentioning
confidence: 99%