[en] In this work X-ray tomography is used to analyse the influence of liquid viscosity on liquid flow in a column filled with Mellapak Plus 752Y structured packing. Tomographic measurements are performed at various column heights for different liquid flow rates. Water and glycerine aqueous solutions are successively used as working liquids in order to quantify the influence of liquid viscosity on hydrodynamic quantities such as liquid hold-up and gas-liquid interfacial area. As expected, both liquid hold-up and gas-liquid interfacial area increase with liquid flow rate. An increase of liquid viscosity has also a positive impact on liquid hold-up and on gas-liquid interfacial area. In all cases, the measured quantities are not constant along the bed height, leading to fluctuating axial profiles. Furthermore, tomographic images are used to identify different liquid flow patterns (films, contact-point liquid, flooded regions) in the irrigated cross section images. A method based on morphological techniques is proposed to quantify the fraction of liquid flow within each flow pattern depending on flow rate and liquid viscosity.
Disciplines :
Chemical engineering
Author, co-author :
Janzen, Anna; University of Paderborn > Chair of Fluid Process Engineering
Steube, Julia; University of Paderborn > Chair of Fluid Process Engineering
Aferka, Saïd; Université de Liège - ULiège > Chimie appliquée > Laboratoire de Génie chimique
Kenig, Evgeny; University of Paderborn > Chair of Fluid Process Engineering
Crine, Michel ; Université de Liège - ULiège > Département de chimie appliquée > Génie chimique - Opérations physiques unitaires
Marchot, Pierre ; Université de Liège - ULiège > Département de chimie appliquée > Département de chimie appliquée
Toye, Dominique ; Université de Liège - ULiège > Département de chimie appliquée > Génie de la réaction et des réacteurs chimiques
Language :
English
Title :
Investigation of liquid flow morphology inside a structured packing using X-ray tomography
Publication date :
2013
Journal title :
Chemical Engineering Science
ISSN :
0009-2509
eISSN :
1873-4405
Publisher :
Pergamon Press - An Imprint of Elsevier Science, Oxford, United Kingdom
Aferka S., Crine M., Saroha A.K., Toye D., Marchot P. In situ measurements of the static liquid holdup in Katapak-SP12 (TM) packed column using X-ray tomography. Chemical Engineering Science 2007, 62:6076-6080.
Aferka S., Marchot P., Crine M., Toye D. Interfacial area measurement in a catalytic distillation packing using high energy X-ray CT. Chemical Engineering Science 2010, 65:511-516.
Aferka S., Viva A., Brunazzi E., Marchot P., Crine M., Toye D. Tomographic measurement of liquid hold up and effective interfacial area distributions in a column packed with high performance structured packings. Chemical Engineering Science 2011, 66:3413-3422.
Billet R., Schultes M. Fluid dynamics and mass transfer in the total capacity range of packed columns up to the flood point. Chemical Engineering & Technology 1995, 18:371-379.
Böcker S., Ronge G. Distillation of viscous systems. Chemical Engineering & Technology 2005, 28:25-28.
Green C.W., Farone J., Briley J.K., Eldridge R.B., Ketcham R.A., Nightingale B. Novel application of X-ray computed tomography: determination of gas/liquid contact area and liquid holdup in structured packing. Industrial & Engineering Chemistry Research 2007, 46:5734-5753.
Marchot P., Toye D., Pelsser A.M., Crine M., L'Homme G., Olujic Z. Liquid distribution images on structured packing by X-ray computed tomography. AIChE Journal 2001, 47:1471-1476.
Nicolaiewsky E.M.A., Fair J.R. Liquid flow over textured surfaces. 1. Contact angles. Industrial and Engineering Chemistry Research 1999, 38:284-291.
Rocha J.A., Bravo J.L., Fair J.R. Distillation columns containing structured packings-a comprehensive model for their performance.1. Hydraulic models. Industrial & Engineering Chemistry Research 1993, 32:641-651.
Rocha J.A., Bravo J.L., Fair J.R. Distillation columns containing structured packings: a comprehensive model for their performance. 2. Mass-transfer model. Industrial & Engineering Chemistry Research 1996, 35:1660-1667.
Schmit C.E., Cartmel D.B., Eldridge R.B. The experimental application of X-ray tomography to a vapor-liquid contactor. Chemical Engineering Science 2001, 56:3431-3441.
Schmit C.E., Eldridge R.B. Investigation of X-ray imaging of vapor-liquid contactors. I. Studies involving stationary objects and a simple flow system. Chemical Engineering Science 2004, 59:1255-1266.
Shi M.G., Mersmann A. Effective interfacial area in packed columns. German Chemical Engineering 1985, 8:87-96.
Shilkin A., Kenig E.Y. A new approach to fluid separation modelling in the columns equipped with structured packings. Chemical Engineering Journal 2005, 110:87-100.
Stoter, F., 1993. Modelling of Maldistribution in Structured Packings: From Detail to Column Design. Ph.D. Thesis. Delft University of Technology.
Suess P., Spiegel L. Hold-up of mellapak structured packings. Chemical Engineering and Processing 1992, 31:119-124.
Toye D., Crine M., Marchot P. Imaging of liquid distribution in reactive distillation packings with a new high-energy X-ray tomograph. Measurement Science & Technology 2005, 16:2213-2220.
Tsai R.E., Seibert A.F., Eldridge R.B., Rochelle G.T. Influence of viscosity and surface tension on the effective mass transfer area of structured packing. Energy Procedia 2009, 1:1197-1204.
Viva A., Aferka S., Brunazzi E., Marchot P., Crine M., Toye D. Processing of X-ray tomographic images: a procedure adapted for the analysis of phase distribution in MellapakPlus 752.Y and Katapak-SP packings. Flow Measurement and Instrumentation 2011, 22:279-290.
Viva A., Aferka S., Toye D., Marchot P., Crine M., Brunazzi E. Determination of liquid hold-up and flow distribution inside modular catalytic structured packings. Chemical Engineering Research & Design 2011, 89:1414-1426.