Analysis of liquid flow distribution in trickle bed reactor using computer assisted tomographyToye, Dominique ; Marchot, Pierre ; Crine, Michel et alin Beck, M. S.; Hoyle, B. S.; Morris, M. A. (Eds.) et al Process tomography - 1995 - Implementation for industrial processes (1995) Detailed reference viewed: 11 (2 ULg) Analysis of liquid flow distribution in a trickle bed reactorToye, Dominique ; Marchot, Pierre ; Crine, Michel et alin Frontiers in Industrial Process Tomography (1995) Detailed reference viewed: 8 (0 ULg)![]() Analysis of Liquid Flow Distribution in Trickling Flow Reactor Using Computer-Assisted X-Ray TomographyToye, Dominique ; Marchot, Pierre ; Crine, Michel et alin Chemical Engineering Research & Design : Transactions of the Institution of Chemical Engineers Part A (1995), 73(A3), 258-262 In this paper, we propose a new experimental technique, based on X-ray tomography, allowing the analysis of the gas-liquid-solid phase distribution in trickling flow reactors. Tomography refers to the ... [more ▼] In this paper, we propose a new experimental technique, based on X-ray tomography, allowing the analysis of the gas-liquid-solid phase distribution in trickling flow reactors. Tomography refers to the cross-sectional imaging of an object from data collected by illuminating this object from many directions. The experimental set-up allows the scanning of transverse sections of rather large columns: up to 0.8 m diameter and 2 m height can be irradiated. Experiments were carried out both without and with liquid flow. In the absence of liquid, the reconstructed images give a view of the non-uniformity of the solid phase distribution. The images obtained are very complex because they result from the superposition of several distributions with different Spatial scales. We show the existence of a first spatial scale which allows us to separate properties belonging to the individual packing elements from those belonging to the bed scale. When liquid is flowing through the packed bed X-ray scans give a clear picture of the distribution of the liquid phase saturation, despite the very low liquid film thickness. Average values of this liquid phase saturation are determined and confronted with a partial wetting model. [less ▲] Detailed reference viewed: 23 (1 ULg)![]() The use of large scale computer assisted tomography for the study of hydrodynamics in trickling filtersToye, Dominique ; Crine, Michel ; Marchot, Pierre et alPoster (1994) Detailed reference viewed: 9 (2 ULg)![]() Trickle flow in packed columns : new experimental and theoretical investigationsCrine, Michel ; Marchot, Pierre ; Toye, Dominique et alin Trends in Chemical Engineering (1994), 2 Detailed reference viewed: 3 (1 ULg)![]() The use of large scale computer assisted tomography for the study of hydrodynamics in trickling filtersToye, Dominique ; Marchot, Pierre ; Crine, Michel et alin Chemical Engineering Science (1994), 49(24B), 5271-5280 In this paper, a new experimental technique is proposed, based on X-ray tomography, allowing the analysis of the gas-liquid-solid phase distribution in trickling filters. Tomography refers to the cross ... [more ▼] In this paper, a new experimental technique is proposed, based on X-ray tomography, allowing the analysis of the gas-liquid-solid phase distribution in trickling filters. Tomography refers to the cross-sectional imaging of an object from data collected by illuminating this object from many directions. The experimental set-up allows the scanning of transverse sections of rather large filters: up to 0.8 m diameter and 2 m height can be irradiated. Experiments were carried out both without and with liquid flow. In the absence of liquid, the reconstructed images give a view of the non-uniformity of the solid phase distribution. The images obtained are very complex because they result from the superposition of several distributions with different spatial scales. The existence of a first spatial scale is shown which allows separation of the properties belonging to the individual packing elements from those belonging to the bed scale. When liquid is flowing through the packed bed, the distribution of the liquid hold-up is clearly evidenced, despite the very low liquid film thickness. [less ▲] Detailed reference viewed: 19 (6 ULg)![]() Macromixing versus hydrodynamics in trickle-flow columnsCrine, Michel ; Marchot, Pierre ; et alin Chemical Engineering Science (1992), 47 Detailed reference viewed: 5 (1 ULg)![]() Rational descriptionthe trickle flow through packed beds. Part I : Liquid distribution far form the distributerMarchot, Pierre ; Crine, Michel ; L'Homme, Guy ![]() in Chemical Engineering (1992), 48 Detailed reference viewed: 5 (1 ULg)![]() Rational description of the trickle flow through packed beds. Part II : Radial spreading of the liquidMarchot, Pierre ; Crine, Michel ; L'Homme, Guy ![]() in Chemical Engineering (1992), 48 Detailed reference viewed: 6 (1 ULg)![]() Statistical hydrodynamics in trickle flow columnsCrine, Michel ; Marchot, Pierre ; L'Homme, Guy ![]() in AIChE Journal (1992), 38 Detailed reference viewed: 13 (2 ULg)![]() Traitement de la fraction organique des ordures ménagères par digestion anaérobie thermophile; ; et al Poster (1991) Detailed reference viewed: 27 (5 ULg)![]() Evaluation of the performances of random plastic media in aerobic trickling filtersCrine, Michel ; ; L'Homme, Guy ![]() in Water Science & Technology (1990), 22 Detailed reference viewed: 17 (3 ULg)![]() Hydrodynamique et distribution de temps de séjour dans les lits bactériensCrine, Michel ; Marchot, Pierre ; et alin Les réacteurs gaz-liquide et gaz-liquide-solide (1990) Detailed reference viewed: 18 (1 ULg)![]() Rôle de la dispersion radiale et du mouillage local sur l'hétérogénéité de l'écoulement de liquide dans un lit bactérien; Crine, Michel ; Marchot, Pierre et alin Tribune de l'Eau (La) (1989), 41 Detailed reference viewed: 10 (2 ULg)![]() Two phase flow through a packed bed : a stochastic model based on the percolation conceptsMarchot, Pierre ; Crine, Michel ; L'Homme, Guy ![]() in Chemical Engineering Journal (1987), 36 Detailed reference viewed: 6 (1 ULg)![]() Utilitation des nodules océaniques polymétalliques en hydrotraitement des coupes pétrolières lourdes avant leur valorisation métallurgiqueDodet, Claude ; Noville, Francis ; Crine, Michel et alin L'industrie minérale - Mines et Carrières - Les techniques (1986), 68 Detailed reference viewed: 29 (6 ULg) Axial dispersion in trickle-flow reactorsCrine, Michel ; L'Homme, Guy ![]() in Enclyclopedia of Fluid Mechanisms (1986) Detailed reference viewed: 8 (0 ULg)![]() Gasification of coal for the generation of electricity in a combined cycle; Pirard, Jean-Paul ; L'Homme, Guy ![]() in Bulletin Scientifique de l'Association des Ingénieurs Electriciens sortis de l'Institut Electrotechnique Montefiore (1985), 2 The article reviews the historical development of processes for the gasification of coal, and discusses the principal chemical reactions employed, describing four principal types of gasifier. It proposes ... [more ▼] The article reviews the historical development of processes for the gasification of coal, and discusses the principal chemical reactions employed, describing four principal types of gasifier. It proposes a scheme for combined-cycle generation consisting of a gasifier, gas turbine, heat exchanger/steam generator, and steam turbine. The economics of the scheme are discussed, concluding that although the forecast unit cost of generation is not excessive, the time is not yet ripe for the installation in Belgium of such schemes on a large scale [less ▲] Detailed reference viewed: 49 (2 ULg)![]() Etude économique des procédés de gazéification du charbon pour la production de SNG; Pirard, Jean-Paul ; L'Homme, Guy ![]() in Revue EPE Energie Primaire (1985), 19 Detailed reference viewed: 19 (0 ULg)![]() Influence of the reactional system on the irrigation rate in trickle-bed reactors; Crine, Michel ; Germain, Albert et alin Chemical and Catalytic Reactor Modelling (1984) Detailed reference viewed: 15 (0 ULg) |
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