Documents disponibles écrits par cet auteur

Double X - ray tomography of a bubbling fluidized bed / R. F. Mudde in Industrial & engineering chemistry research, Vol. 49 N° 11 (Juin 2010) 

Public ISBD [article]  in Industrial & engineering chemistry research > Vol. 49 N° 11 (Juin 2010) . - pp. 5061–5065 Titre : Double X - ray tomography of a bubbling fluidized bed Type de document : texte imprimé Auteurs : R. F. Mudde, Auteur Année de publication : 2010 Article en page(s) : pp. 5061–5065 Note générale : Industrial chemistry Langues : Anglais (eng) Mots-clés : X-ray  tomography  Fluidized  bed Résumé : This paper discusses the measurement of bubbles moving through a fluidized bed imaged with a double X-ray tomographic scanner. The scanner is made of 3 X-ray sources equipped with two rings of 90 CdWO4 detectors. The fluidized bed has a diameter of 23 cm and is filled with a Geldart B powder. The scanner measures the attenuation in two thin parallel slices separated by a small vertical distance. This allows the estimate of the velocity of individual bubbles rising through the bed. Data are collected at a frequency of 2500 Hz. To remove the noise, data are averaged over 10 samples before tomographic reconstruction is performed, resulting in 250 independent frames per second. From the measured bubble velocity and the passage time through the reconstruction planes, the vertical dimensions of the bubbles are found. This allows imaging of the real shape of the bubbles and calculation of the volume of each individual bubble. ISSN : 0888-5885 En ligne : http://pubs.acs.org/doi/abs/10.1021/ie901537z [article] Double X - ray tomography of a bubbling fluidized bed [texte imprimé] / R. F. Mudde, Auteur . - 2010 . - pp. 5061–5065. Industrial chemistry Langues : Anglais (eng) in Industrial & engineering chemistry research > Vol. 49 N° 11 (Juin 2010) . - pp. 5061–5065 Mots-clés : X-ray  tomography  Fluidized  bed Résumé : This paper discusses the measurement of bubbles moving through a fluidized bed imaged with a double X-ray tomographic scanner. The scanner is made of 3 X-ray sources equipped with two rings of 90 CdWO4 detectors. The fluidized bed has a diameter of 23 cm and is filled with a Geldart B powder. The scanner measures the attenuation in two thin parallel slices separated by a small vertical distance. This allows the estimate of the velocity of individual bubbles rising through the bed. Data are collected at a frequency of 2500 Hz. To remove the noise, data are averaged over 10 samples before tomographic reconstruction is performed, resulting in 250 independent frames per second. From the measured bubble velocity and the passage time through the reconstruction planes, the vertical dimensions of the bubbles are found. This allows imaging of the real shape of the bubbles and calculation of the volume of each individual bubble. ISSN : 0888-5885 En ligne : http://pubs.acs.org/doi/abs/10.1021/ie901537z

Uniform flow in bubble columns / R. F. Mudde in Industrial & engineering chemistry research, Vol. 48 N°1 (Janvier 2009) 

Public ISBD [article]  in Industrial & engineering chemistry research > Vol. 48 N°1 (Janvier 2009) . - p. 148-158 Titre : Uniform flow in bubble columns Type de document : texte imprimé Auteurs : R. F. Mudde, Editeur scientifique ; W. K. Harteveld, Editeur scientifique ; H. E. A van den Akker, Editeur scientifique Année de publication : 2009 Article en page(s) : p. 148-158 Note générale : Chemical engineering Langues : Anglais (eng) Mots-clés : Flow  in  Bubble  Columns  Optical  glass  fibers  Liquid  axial  velocity  field  Gas Résumé : Uniform bubbly flow in a 15 cm bubble column is investigated. We use a special needle sparger consisting of 559 separate needles, uniformly distributed over the bottom. With this sparger, we can ensure that all bubbles generated are of the same size and that the bubble injection is very uniform over the entire bottom of the column. Detailed experiments are reported, using optical glass fibers to measure the local gas fraction and bubble size and velocity and using laser Doppler anemometry to measure the liquid axial velocity field. We find that the homogeneous flow regime extends up to a gas fraction of 55% well beyond the predictions of theory. The superficial gas velocity at which the homogeneous regime looses its stability depends on the water quality: fresh water looses its stability much earlier than old water. However, the gas fraction as a function of the superficial gas velocity is in the homogeneous regime independent of the water quality. The overall gas fraction can be described by a Richardson and Zaki type of relation or by the proposal by Garnier et al. We have indications that, at the point of instability, the bubble size has increased to a critical value at which the lift force reverses sign. This causes the radial gas fraction to change from flat with a small wall peaking to core peaking provoking the instability as suggested by Lucas et al. [ Chem. Eng. Technol. 2005, 60, 3609]. Alternatively, at higher gas fractions, the swarm gets denser and the bubble wakes get suppressed. According to Fox and co-workers [ Chem. Eng. Sci. 2007, 62, 3159], this causes the flow to lose its stability. En ligne : http://pubs.acs.org/doi/abs/10.1021/ie8000748 [article] Uniform flow in bubble columns [texte imprimé] / R. F. Mudde, Editeur scientifique ; W. K. Harteveld, Editeur scientifique ; H. E. A van den Akker, Editeur scientifique . - 2009 . - p. 148-158. Chemical engineering Langues : Anglais (eng) in Industrial & engineering chemistry research > Vol. 48 N°1 (Janvier 2009) . - p. 148-158 Mots-clés : Flow  in  Bubble  Columns  Optical  glass  fibers  Liquid  axial  velocity  field  Gas Résumé : Uniform bubbly flow in a 15 cm bubble column is investigated. We use a special needle sparger consisting of 559 separate needles, uniformly distributed over the bottom. With this sparger, we can ensure that all bubbles generated are of the same size and that the bubble injection is very uniform over the entire bottom of the column. Detailed experiments are reported, using optical glass fibers to measure the local gas fraction and bubble size and velocity and using laser Doppler anemometry to measure the liquid axial velocity field. We find that the homogeneous flow regime extends up to a gas fraction of 55% well beyond the predictions of theory. The superficial gas velocity at which the homogeneous regime looses its stability depends on the water quality: fresh water looses its stability much earlier than old water. However, the gas fraction as a function of the superficial gas velocity is in the homogeneous regime independent of the water quality. The overall gas fraction can be described by a Richardson and Zaki type of relation or by the proposal by Garnier et al. We have indications that, at the point of instability, the bubble size has increased to a critical value at which the lift force reverses sign. This causes the radial gas fraction to change from flat with a small wall peaking to core peaking provoking the instability as suggested by Lucas et al. [ Chem. Eng. Technol. 2005, 60, 3609]. Alternatively, at higher gas fractions, the swarm gets denser and the bubble wakes get suppressed. According to Fox and co-workers [ Chem. Eng. Sci. 2007, 62, 3159], this causes the flow to lose its stability. En ligne : http://pubs.acs.org/doi/abs/10.1021/ie8000748