Loughborough University
Leicestershire, UK
LE11 3TU
+44 (0)1509 263171
Loughborough University

Loughborough University Institutional Repository

Please use this identifier to cite or link to this item: https://dspace.lboro.ac.uk/2134/7676

Title: Experimental study of void fraction behaviour in vertical bubbly gas-liquid flow using conductivity and measurements
Authors: Al-Oufi, Fahd M.
Rielly, Chris D.
Cumming, Iain W.
Keywords: Annulus
Gas hold-up
Gas-liquid flow
Ring electrode
Issue Date: 2007
Publisher: © The Administration of Saudi Clubs and Schools in the UK and Ireland, Term 26th
Citation: AL-OUFI, F.M., RIELLY, C.D. and CUMMING, I.W., 2007. Experimental study of void fraction behaviour in vertical bubbly gas-liquid flow using conductivity and measurements. IN: Al-Yami, A.M. (ed.). Proceedings of the Saudi Innovation Conference, Newcastle-upon-Tyne, United Kingdom, 11th- 12th May, pp. 178-186.
Abstract: The void fraction is an important variable in describing gas-liquid two-phase flows, since it is required to predict the heat and mass transfer coefficients and the pressure drop and is an indicator of the flow regime. The contrast in conductivity between water and air is one way to measure the void fraction in gas-liquid flow. This project has examined use of the ring conductivity electrodes to measuring the void fraction in an up-flow bubble column. The conductivity method has potential to be a low cost, safe and accurate method of measuring local void fractions in pipes and other process engineering mass transfer devices. In this project, the void fraction was measured in an air-water system by using conductivity in a 2" pipe equipped with two ring electrodes. Further gas hold-up experiments were conducted in the annular channel formed between 2" and a 4" pipe, using a system of four pairs of electrodes. The data obtained from the experiments agreed fairly well with the Maxwell and Burggeman theories which relate the dimensionless conductance to the void fraction. The measured void fractions were correlated using the drift-flux model, as proposed by Zuber and Findlay. Significant differences were observed between the void fraction measurements obtained for the annular channel and for an empty pipe, when operated at the same gas superficial velocity.
Description: This is a conference paper.
Version: Accepted for publication
URI: https://dspace.lboro.ac.uk/2134/7676
Publisher Link: http://saudistudents.tripod.com/
ISBN: 9780955104923
Appears in Collections:Conference Papers and Presentations (Chemical Engineering)

Files associated with this item:

File Description SizeFormat


SFX Query

Items in DSpace are protected by copyright, with all rights reserved, unless otherwise indicated.