An engineering model for dilute riser flow.

J.J. Nieuwland, J.J. Nieuwland, E. Delnoij, J.A.M. Kuipers, Willibrordus Petrus Maria van Swaaij

Research output: Contribution to journalArticleAcademicpeer-review

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Abstract

To facilitate understanding of the hydrodynamic behaviour of CFBs, a one-dimensional model for the riser tube of a CFB has been developed. The model describes steady state hydrodynamic key variables (i.e. cross-sectional averaged values of pressure, solids concentration and velocities of both phases) for developing axi-symmetrical flow as a function of the axial position in the riser tube. Calculated results have been compared with experimental data obtained from a small scale CFB unit which could be operated at pressures up to 6 bar. Despite the simplicity of the model, it turned out that the model was capable of predicting the effect of changes in operating conditions (i.e. gas velocity, solids mass flux, operating pressure and particle diameter). The model neglects the existence of clustering of particles, lateral solids segregation and solids downflow near the tube wall, which limits the applicability to dilute systems (εs<0.04).
Original languageUndefined
Pages (from-to)115-123
Number of pages9
JournalPowder technology
Volume90
Issue number2
DOIs
Publication statusPublished - 1997

Keywords

  • METIS-106392
  • IR-11897

Cite this

Nieuwland, J. J., Nieuwland, J. J., Delnoij, E., Kuipers, J. A. M., & van Swaaij, W. P. M. (1997). An engineering model for dilute riser flow. Powder technology, 90(2), 115-123. https://doi.org/10.1016/S0032-5910(96)03205-6
Nieuwland, J.J. ; Nieuwland, J.J. ; Delnoij, E. ; Kuipers, J.A.M. ; van Swaaij, Willibrordus Petrus Maria. / An engineering model for dilute riser flow. In: Powder technology. 1997 ; Vol. 90, No. 2. pp. 115-123.
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title = "An engineering model for dilute riser flow.",
abstract = "To facilitate understanding of the hydrodynamic behaviour of CFBs, a one-dimensional model for the riser tube of a CFB has been developed. The model describes steady state hydrodynamic key variables (i.e. cross-sectional averaged values of pressure, solids concentration and velocities of both phases) for developing axi-symmetrical flow as a function of the axial position in the riser tube. Calculated results have been compared with experimental data obtained from a small scale CFB unit which could be operated at pressures up to 6 bar. Despite the simplicity of the model, it turned out that the model was capable of predicting the effect of changes in operating conditions (i.e. gas velocity, solids mass flux, operating pressure and particle diameter). The model neglects the existence of clustering of particles, lateral solids segregation and solids downflow near the tube wall, which limits the applicability to dilute systems (εs<0.04).",
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author = "J.J. Nieuwland and J.J. Nieuwland and E. Delnoij and J.A.M. Kuipers and {van Swaaij}, {Willibrordus Petrus Maria}",
year = "1997",
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volume = "90",
pages = "115--123",
journal = "Powder technology",
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Nieuwland, JJ, Nieuwland, JJ, Delnoij, E, Kuipers, JAM & van Swaaij, WPM 1997, 'An engineering model for dilute riser flow.', Powder technology, vol. 90, no. 2, pp. 115-123. https://doi.org/10.1016/S0032-5910(96)03205-6

An engineering model for dilute riser flow. / Nieuwland, J.J.; Nieuwland, J.J.; Delnoij, E.; Kuipers, J.A.M.; van Swaaij, Willibrordus Petrus Maria.

In: Powder technology, Vol. 90, No. 2, 1997, p. 115-123.

Research output: Contribution to journalArticleAcademicpeer-review

TY - JOUR

T1 - An engineering model for dilute riser flow.

AU - Nieuwland, J.J.

AU - Nieuwland, J.J.

AU - Delnoij, E.

AU - Kuipers, J.A.M.

AU - van Swaaij, Willibrordus Petrus Maria

PY - 1997

Y1 - 1997

N2 - To facilitate understanding of the hydrodynamic behaviour of CFBs, a one-dimensional model for the riser tube of a CFB has been developed. The model describes steady state hydrodynamic key variables (i.e. cross-sectional averaged values of pressure, solids concentration and velocities of both phases) for developing axi-symmetrical flow as a function of the axial position in the riser tube. Calculated results have been compared with experimental data obtained from a small scale CFB unit which could be operated at pressures up to 6 bar. Despite the simplicity of the model, it turned out that the model was capable of predicting the effect of changes in operating conditions (i.e. gas velocity, solids mass flux, operating pressure and particle diameter). The model neglects the existence of clustering of particles, lateral solids segregation and solids downflow near the tube wall, which limits the applicability to dilute systems (εs<0.04).

AB - To facilitate understanding of the hydrodynamic behaviour of CFBs, a one-dimensional model for the riser tube of a CFB has been developed. The model describes steady state hydrodynamic key variables (i.e. cross-sectional averaged values of pressure, solids concentration and velocities of both phases) for developing axi-symmetrical flow as a function of the axial position in the riser tube. Calculated results have been compared with experimental data obtained from a small scale CFB unit which could be operated at pressures up to 6 bar. Despite the simplicity of the model, it turned out that the model was capable of predicting the effect of changes in operating conditions (i.e. gas velocity, solids mass flux, operating pressure and particle diameter). The model neglects the existence of clustering of particles, lateral solids segregation and solids downflow near the tube wall, which limits the applicability to dilute systems (εs<0.04).

KW - METIS-106392

KW - IR-11897

U2 - 10.1016/S0032-5910(96)03205-6

DO - 10.1016/S0032-5910(96)03205-6

M3 - Article

VL - 90

SP - 115

EP - 123

JO - Powder technology

JF - Powder technology

SN - 0032-5910

IS - 2

ER -