2013
DOI: 10.1016/j.ces.2013.08.050
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Sub-grid drag models for horizontal cylinder arrays immersed in gas-particle multiphase flows

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Cited by 25 publications
(24 citation statements)
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“…Many subgrid drag modifications have, therefore, been put forth by academic researchers to account for the effect of small unresolved scales on the resolved meso‐scales in this case . Recently, the comparative study of Schneiderbauer et al revealed that although these drag modifications cited above show considerably different dependencies, they are able to predict main features of the gas and particle flow in bubbling fluidized beds adequately.…”
Section: Introductionmentioning
confidence: 99%
“…Many subgrid drag modifications have, therefore, been put forth by academic researchers to account for the effect of small unresolved scales on the resolved meso‐scales in this case . Recently, the comparative study of Schneiderbauer et al revealed that although these drag modifications cited above show considerably different dependencies, they are able to predict main features of the gas and particle flow in bubbling fluidized beds adequately.…”
Section: Introductionmentioning
confidence: 99%
“…Additionally we define two characteristic values used to non-dimensionalize quantities: a length and a velocity. These characteristic values are based on the solids terminal velocity v t , which has been shown to describe the hydrodynamics of the suspension well in previous gas-particle filtering studies, such as Igci et al (gas-particle hydrodynamics) [3], Sarkar et al (gas-particle hydrodynamics with immersed cylinders) [7], Holloway and Sundaresan (reacting gas-particle flows) [10], and Agrawal et al (gas-particle scalar transport) [9]. The characteristic values are also defined in Table 2.…”
Section: Simulation Setupmentioning
confidence: 79%
“…More recently, such sub-grid methods have been extended to simulate gas-particle flows; filtered models have been developed for interphase drag [3][4][5][6], cylinder-suspension drag [7,8], interphase heat transfer [9], and reactive flows [10]. While these filtered-model simulations reduce the ability to predict fine-scale behavior, they can predict bulk flow behavior of large-scale devices with reasonable accuracy and significant computational savings.…”
Section: Introductionmentioning
confidence: 99%
“…29,30 Submodels that capture kinetic and thermodynamic data can also be incorporated for subsequent optimization of processes, as carried out by the CCSI Toolset. 16 More detailed simulations, such as those that use filtered constitutive relationships in coarse-grid computational fluid dynamics (CFD) simulations which may better capture the multi-scale nature inside processes such as fluidized beds, [31][32][33] can be used to refine the process design, a challenging task that has not been attained at this point. 16 Furthermore, at the process level, several studies simulated and optimized the pressure-swing adsorption (PSA) process for CO 2 sequestration 34 and used superstructure based methods to design PSA cycle configurations.…”
Section: Co 2 Capture Utilization and Storagementioning
confidence: 99%