Investigation on liquid maldistribution in packed beds by X-ray tomographyMarchot, Pierre ; Toye, Dominique ; Crine, Michel et alin Chemical Engineering Research & Design : Transactions of the Institution of Chemical Engineers Part A (1999), 77 Detailed reference viewed: 4 (1 ULg) Modelling of the liquid distribution in a trickle flow packed column based upon X-ray tomography imagesToye, Dominique ; Marchot, Pierre ; Crine, Michel et alin Chemical Engineering Communications (1999), 175 X-ray tomography is used to characterise the liquid distribution in a 0.6 meter diameter and 2 meter height column filled with gas-liquid absorption polypropylene packing elements (Cascade Mini-Ring 1A ... [more ▼] X-ray tomography is used to characterise the liquid distribution in a 0.6 meter diameter and 2 meter height column filled with gas-liquid absorption polypropylene packing elements (Cascade Mini-Ring 1A, Glitsch Benelux). The liquid holdup distribution is determined for liquid flowrates ranging from 1000 l/h to 6000 l/h, that correspond to superficial velocities ranging from 10(-3) to 6 10(-3) m/s, in several cross sections situated at different heights in the packed column. A characteristic length, corresponding to the smallest scale beyond which the packing properties may be supposed statistically homogenous and isotropic, as determined by Means of the autocorrelation function method applied to the images of the solid distribution. Both local and global liquid holdup measurements are satisfactorily modelled by means of a partial wetting model based on a probabilistic approach. [less ▲] Detailed reference viewed: 17 (3 ULg) Trickle flow through packed beds : Use of systemic models in the interpretation of X-ray tomogramsToye, Dominique ; Marchot, Pierre ; Crine, Michel et alConference (1998, August) Detailed reference viewed: 6 (2 ULg) Local measurements of void fraction and liquid holdup in packed columns using X-ray computed tomographyToye, Dominique ; Marchot, Pierre ; Crine, Michel et alin Chemical Engineering & Processing (1998), 37(6), 511-520 A 'tailor made' computed X-ray tomographic scanner has been developed as a tool for the analysis of the distribution of gas, liquid and solid phases in packed columns. The very good spatial resolution of ... [more ▼] A 'tailor made' computed X-ray tomographic scanner has been developed as a tool for the analysis of the distribution of gas, liquid and solid phases in packed columns. The very good spatial resolution of the scanner has first been assessed by the imaging of objects of known shape and size, called 'physical' phantoms. Images have then been realized on a 0.6 m diameter and 2 m height column packed with Cascade Mini-Ring 1A packing elements, which is a random polypropylene packing designed to be used in absorption columns. The solid phase distribution, leading to the void fraction distribution, has been analyzed on cross-section images of the dry packed column (without any liquid flowrate). The measured value of the bed void fraction is equal to the value provided by the manufacturer. The analysis of the axial profile of void fraction shows that the 'end effect' may be neglected, whereas the analysis of the radial profile evidences the existence of a non negligible 'wall effect'. Images have then been carried out on the packed column irrigated by a liquid flowrate ranging between 0 and 6000 1 h(-1) (0-6.10(-3) m s(-1)). Hold-up values have been measured in different cross-sections of the column and averaged in order to obtain the total hold-up value in the bed. The computed values are in very good agreement with those reported in the literature for similar packing. The dependence of the liquid hold-up on the liquid superficial velocity can be expressed in terms of a power law. The fitted value of the exponent, equal to 0.65, is in the range of exponent values found in correlations of the literature. (C) 1998 Elsevier Science S.A. All rights reserved. [less ▲] Detailed reference viewed: 41 (2 ULg) Investigating trickle flow in packed columns by X-ray tomographyToye, Dominique ; Marchot, Pierre ; Crine, Michel et alConference (1997, October) Detailed reference viewed: 8 (2 ULg) X-ray tomography in random packingsToye, Dominique ; Crine, Michel ; Marchot, Pierre ![]() Scientific conference (1997, September 30) Detailed reference viewed: 5 (0 ULg) Perspectives d'utilisation de la tomographie dans la description du fonctionnement des réacteurs à trois phasesToye, Dominique ; Crine, Michel ; Marchot, Pierre et alScientific conference (1997, June 19) Detailed reference viewed: 4 (0 ULg) Modelling of the liquid distribution in a packed column based upon X-ray tomography imagesToye, Dominique ; Marchot, Pierre ; Crine, Michel et alConference (1997) Detailed reference viewed: 11 (2 ULg) Modeling of the liquid phase distribution in a packed column based on the analysis of X-ray tomography imagesToye, Dominique ; Marchot, Pierre ; Crine, Michel et alPoster (1997) Detailed reference viewed: 3 (1 ULg) Oxydation photochimique de lixiviats de décharge; ; Crine, Michel ![]() in Tribune de l'Eau (La) (1997), 590-591 Detailed reference viewed: 32 (3 ULg) Investigating the liquid distribution in a reactive distillation packing using high energy X-ray tomography; Aferka, Saïd ; Crine, Michel et alConference (1996) Detailed reference viewed: 9 (2 ULg) L'hydrodynamique dans les lits bactériens : le rôle du garnissageCrine, Michel ; Toye, Dominique ; Marchot, Pierre ![]() Conference (1996) Detailed reference viewed: 32 (1 ULg) Production of sulfur from gypsum as an industrial byproductHiligsmann, Serge ; ; et alin Applied Biochemistry and Biotechnology (1996), 57-8 Biological sulfate reduction was investigated at the bench and pilot scales in order to determine optimum culture conditions. Efficient strains of sulfate-reducing bacteria (SRB) were selected by ... [more ▼] Biological sulfate reduction was investigated at the bench and pilot scales in order to determine optimum culture conditions. Efficient strains of sulfate-reducing bacteria (SRB) were selected by classical microbiological methods and by mutagenesis. Improvement factors, including stripping, scale-up, sulfate,and organic substrate concentrations, have been studied in batch bioreactors. Two types of pilot-scale bioreactors have been adopted, the first being completely mixed with free cells and the second having two stages with immobilized cells on a fixed bed. An overall bioconversion capacity of 11 kg/m(3) . d of gypsum and 1.2 kg/m(3) . d of dissolved organic carbon has been achieved in the two-stage bioreactor. [less ▲] Detailed reference viewed: 39 (7 ULg) Computer-assisted tomography for liquid imaging in trickle-flow columnsToye, Dominique ; Marchot, Pierre ; Crine, Michel et alin Non-invasive Monitoring of Multiphase Flows (1996) Detailed reference viewed: 8 (0 ULg) Treatment of gypsum waste in a two stage anaerobic reactor; Salmon, Thierry ; Hiligsmann, Serge et alin Water Science & Technology (1996), 34(5-6), 367-374 The reduction of high concentrations of gypsum (up to 110 kg/m(3)) is investigated in a two stage immobilised cell bioreactor. The first stage is mainly colonised by a consortium of acidogenic bacteria ... [more ▼] The reduction of high concentrations of gypsum (up to 110 kg/m(3)) is investigated in a two stage immobilised cell bioreactor. The first stage is mainly colonised by a consortium of acidogenic bacteria and sulphate reducing bacteria oxidising volatile fatty acids with more than 2 carbons (mainly, butyrate and propionate). The gypsum consumption rate is rather high (ii kg/m(3).day). Most of acetate remains unconverted in this first stage. It is partially converted in the second stage (residence time : 12 days) which is predominantly colonised by acetate oxidising bacteria The gypsum consumption rate is much lower than in the first stage : 3 kg/m(3).day. With both stages, it is possible to reach an almost complete conversion of gypsum with an overall capacity of 6.1 kg gypsum/m(3).day. We propose also a very simple model to describe the different transformation rates. It allows us to clearly identify the activity levels of the different types of sulphate reducing bacteria in both stages. Copyright (C) 1996 IAWQ. [less ▲] Detailed reference viewed: 48 (5 ULg) Modelling of multiphase flow in packed beds by computer-assisted x-ray tomographyToye, Dominique ; Marchot, Pierre ; Crine, Michel et alin Measurement Science & Technology (1996), 7(3), 436-443 The high resolution which can be obtained by computer-assisted x-ray tomography is used to investigate Various scale heterogeneities of the flow texture characterizing multiphase flow in packed beds. The ... [more ▼] The high resolution which can be obtained by computer-assisted x-ray tomography is used to investigate Various scale heterogeneities of the flow texture characterizing multiphase flow in packed beds. The direct counting of 'irrigated' pixels allows the determination of the number of individual liquid rivulets as well as their size. The evolution of the liquid flow texture versus the liquid velocity agrees quite well with the predictions of a percolation-based model. This agreement is further confirmed by the comparison of the experimental hold-up values averaged over the column cross-section with the theoretical model. [less ▲] Detailed reference viewed: 16 (2 ULg) Production of sulfur from gypsum as an industrial by-product.Hiligsmann, Serge ; ; et alPoster (1995, May) Detailed reference viewed: 10 (1 ULg) Saturation of Penicillin-Binding Protein 1 by Beta-Lactam Antibiotics in Growing Cells of Bacillus LicheniformisLepage, Sylvie ; Lakaye, Bernard ; Galleni, Moreno et alin Molecular Microbiology (1995), 16(2), 365-72 With the help of a new highly sensitive method allowing the quantification of free penicillin-binding proteins (PBPs) and of an integrated mathematical model, the progressive saturation of PBP1 by various ... [more ▼] With the help of a new highly sensitive method allowing the quantification of free penicillin-binding proteins (PBPs) and of an integrated mathematical model, the progressive saturation of PBP1 by various beta-lactam antibiotics in growing cells of Bacillus licheniformis was studied. Although the results confirmed PBP1 as a major lethal target for these compounds, they also underlined several weaknesses in our present understanding of this phenomenon. In growing cells, but not in resting cells, the penicillin target(s) appeared to be somewhat protected from the action of the inactivators. In vitro experiments indicated that amino acids, peptides and depsipeptides mimicking the peptide moiety of the nascent peptidoglycan significantly interfered with the acylation of PBP1 by the antibiotics. In addition, the level of PBP1 saturation at antibiotic concentrations corresponding to the minimum inhibitory concentrations was not constant, suggesting that additional, presently undiscovered, factors might be necessary to account for the experimental observations. [less ▲] Detailed reference viewed: 26 (2 ULg) In activation of cellulases in stirred bioreactors : solution of the problem and scale-up rules.; ; Crine, Michel et alPoster (1995, February) Detailed reference viewed: 3 (0 ULg) Computer assisted X-ray tomography : a tool for fluid distribution analysis in trickle-bed reactorsCrine, Michel ; Toye, Dominique ; et alConference (1995) Detailed reference viewed: 9 (2 ULg) |
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