The Second China Energy Scientist Forum (CESF 2010 E-BOOK)

Xuzhou,China,10.18-10.19,2010

ISBN: 978-1-935068-37-2 Scientific Research Publishing, USA

E-Book 2244pp Pub. Date: October 2010

Category: Medicine & Healthcare

Price: $360

Title: Phase Separation of Gas-Liquid Two-Phase Flows in Multi-tube T-Junction Separators
Source: The Second China Energy Scientist Forum (CESF 2010 E-BOOK) (pp 241-245)
Author(s): Limin Yang, School of Chemistry and Chemical Engineering, Changzhou University Changzhou, Jiangsu 213164, China
Zhenying Zhao, School of Chemistry and Chemical Engineering, Changzhou University Changzhou, Jiangsu 213164, China
Pengcheng Qi, School of Chemistry and Chemical Engineering, Changzhou University Changzhou, Jiangsu 213164, China
Lili Zhao, School of Chemistry and Chemical Engineering, Changzhou University Changzhou, Jiangsu 213164, China
Barry J. azzopardi, Process and Environmental Engineering Research Division, Faculty of Engineering, University of Nottingham University Park, Nottingham NG7 2RD, UK
Abstract: A simple T-junction can be used as a partial phase separator for gas/liquid flows, but its separation efficiency is low. A multi-tube T-junction separator consists of several T-junctions in one unit in order to improve the separation efficiency. Using air and water as working fluids, separation experiments were carried out with a simple T-junction and with multi-tube T-junction separators with a horizontal main pipe and vertically upward branch(es) with stratified and plug flow at inlet. The results show that for these two flow patterns the separation efficiency of the two phases for any multi-tube T-junction separator is much higher than that of the corresponding T-junction. Increasing the number of connecting tubes in the multi-tube T-junction separator can increase the separation efficiency. Generally, for stratified flows and plug flows, complete separation of the two phases can be achieved by the multi-tube T-junction separator with 5 or more connecting tubes; increasing the gas or the liquid flow rate will be detrimental to two phase separation with a drop in peak separation efficiency.
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