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Original Articles

Eulerian Model for Prediction of Particle Transport and Deposition in Turbulent Duct Flows with Thermophoresis

Pages 802-815 | Received 27 Dec 2014, Accepted 29 Jun 2015, Published online: 14 Aug 2015

Figures & data

FIG. 1. Profiles of in fully developed turbulent flow for particle response times τ+p = 0.2, 1, 5, and 25, from the turbulent channel-flow simulations of Picciotto et al. (Citation2005) at Reτ = 150.

FIG. 1. Profiles of in fully developed turbulent flow for particle response times τ+p = 0.2, 1, 5, and 25, from the turbulent channel-flow simulations of Picciotto et al. (Citation2005) at Reτ = 150.

FIG. 2. Profiles of in the near-wall region of fully developed turbulent flow for particle response times τ+p = 0, 2.5, 5, and 10, calculated as solutions to Equation (Equation8), with Equation (Equation9) as the initial condition.

FIG. 2. Profiles of in the near-wall region of fully developed turbulent flow for particle response times τ+p = 0, 2.5, 5, and 10, calculated as solutions to Equation (Equation8[8] ), with Equation (Equation9[9] ) as the initial condition.

FIG. 3. Turbophoretic particle deposition velocity V+dep in turbulent channel flow, as a function of the particle relaxation timescale τ+p, for the model predictions of Equation (Equation16) and the experimental data of Liu and Agarwal (Citation1974): × at Re = 10, 000 and + at Re = 50, 000.

FIG. 3. Turbophoretic particle deposition velocity V+dep in turbulent channel flow, as a function of the particle relaxation timescale τ+p, for the model predictions of Equation (Equation16[16] ) and the experimental data of Liu and Agarwal (Citation1974): × at Re = 10, 000 and + at Re = 50, 000.

FIG. 4. (a) The particle mass flux boundary condition applied at the pipe surface. (b) The mixed-mean temperature as a function of cooling-section inlet temperature Tin in the heated pipe-flow experiments of Romay et al. (Citation1998).

FIG. 4. (a) The particle mass flux boundary condition applied at the pipe surface. (b) The mixed-mean temperature as a function of cooling-section inlet temperature Tin in the heated pipe-flow experiments of Romay et al. (Citation1998).

FIG. 5. Deposition efficiency η of NaCl particles as a function of cooling-section inlet temperature Tin in laminar pipe flow at Re = 1397. Solid lines describe model predictions and symbols denote the experimental data of Romay et al. (Citation1998).

FIG. 5. Deposition efficiency η of NaCl particles as a function of cooling-section inlet temperature Tin in laminar pipe flow at Re = 1397. Solid lines describe model predictions and symbols denote the experimental data of Romay et al. (Citation1998).

FIG. 6. Deposition efficiency η of NaCl particles as a function of cooling-section inlet temperature Tin in pipe flow at Re = 5517. Solid lines describe model predictions and symbols denote the experimental data of Romay et al. (Citation1998).

FIG. 6. Deposition efficiency η of NaCl particles as a function of cooling-section inlet temperature Tin in pipe flow at Re = 5517. Solid lines describe model predictions and symbols denote the experimental data of Romay et al. (Citation1998).

FIG. 7. Deposition efficiency η of NaCl particles as a function of cooling-section inlet temperature Tin in pipe flow at Re = 9656. Solid lines describe model predictions and symbols denote the experimental data of Romay et al. (Citation1998).

FIG. 7. Deposition efficiency η of NaCl particles as a function of cooling-section inlet temperature Tin in pipe flow at Re = 9656. Solid lines describe model predictions and symbols denote the experimental data of Romay et al. (Citation1998).

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