Analytical solution and experimental measurements for temperature distribution prediction of three-phase direct-contact condenser

被引:23
|
作者
Mahood, Hameed B. [1 ,2 ]
Sharif, A. O. [1 ,3 ]
Al-Aibi, S. [1 ]
Hawkins, D. [1 ]
Thorpe, R. [1 ]
机构
[1] Univ Surrey, Fac Engn & Phys Sci, Chem & Proc Engn Dept, Ctr Osmosis Res & Applicat, Guildford GU2 7XH, Surrey, England
[2] Univ Misan, Misan, Iraq
[3] Qatar Fdn, Qatar Energy & Environm Res Inst, Doha, Qatar
关键词
Direct-contact heat transfer; Three-phase condenser; Analytical modelling; Experimental measurements; Temperature distributions; HEAT-TRANSFER; NONCONDENSABLE GAS; IMMISCIBLE LIQUID; POTENTIAL FLOW; SPRAY-COLUMN; PHASE; BUBBLES; MODEL;
D O I
10.1016/j.energy.2013.12.026
中图分类号
O414.1 [热力学];
学科分类号
摘要
An experimental and analytical investigation for the temperature distribution prediction of a three-phase bubble-type direct-contact condenser conducted, using a short Perspex column with 4 cm internal diameter and 70 cm height as a direct contact condenser. Vapour pentane and water were exploited as dispersed phase and continuous phase respectively. The effect of mass flow rate ratio (43.69%, 22.97%, 12.23%, 8.61% and 6.46%) and initial dispersed phase temperature (37.6 degrees C, 38.4 degrees C and 41.7 degrees C) on the direct contact condenser output were studied. Linear temperature distributions along direct contact condensers were found experimentally, except at mass flow rate ratio 43.69% and with less magnitude at 22.97%, for different initial vapour temperatures, while theoretically this behaviour is purely linear. The results showed that the mass flow rate ratio and the hold up have a dominant effect on the direct contact condenser output. On the other hand, the initial vapour temperature had a slight effect on the direct contact condenser output temperature which indicates that the latent heat is controlled in the exchange process. The analytical model is based on the one-dimensional mass and energy equations. New expressions for average heat transfer coefficient and two-phase bubbles relative velocity are derived implicitly. Furthermore, the model correlated very well against experimental data obtained. (C) 2013 Elsevier Ltd. All rights reserved.
引用
收藏
页码:538 / 547
页数:10
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