Experimental characterization of heat transfer enhancement in a circular tube fitted with Koflo Blade™ inline mixer

被引:16
作者
Zarei, Ramin [1 ]
Razzaghi, Kiyanoosh [1 ]
Shahraki, Farhad [1 ]
机构
[1] Univ Sistan & Baluchestan, Dept Chem Engn, Heat & Fluid Flow Lab, Zahedan 98164161, Iran
关键词
Inline mixer; Heat transfer enhancement; Swirl flow; Nusselt number; Friction factor; PRESSURE-DROP CORRELATIONS; TWISTED-TAPE INSERTS; NANOFLUID FLOW; LAMINAR-FLOW; ISOTHERMAL TUBES; STATIC MIXERS; SWIRL FLOW; EXCHANGERS; AUGMENTATION; PERFORMANCE;
D O I
10.1016/j.cep.2021.108508
中图分类号
TE [石油、天然气工业]; TK [能源与动力工程];
学科分类号
0807 ; 0820 ;
摘要
This paper addresses the experimental study of heat transfer enhancement of laminar flow in a tube fitted with Koflo Blade (TM) inline mixer as the swirl-flow generator and under constant surface heat flux. Experiments were carried out with air as heat transfer fluid and two different types of the mixer having blades crossing angles of 90 degrees and 120 degrees The flow swirling in the mixer is mainly due to the centrifugal force induced by the angle between the blades, which is responsible for heat transfer augmentation. The results show that the mixer with 90 degrees blades supplies Nusselt numbers higher than the 120 degrees mixer but, likewise, results in higher pressure drop. The rate of heat transfer in the tube equipped with inserts was augmented up to 78% and 47% for 90 degrees-blades and 120 degrees-blades mixers, respectively. The enhancement in heat transfer was correlated with the Graetz number that supports the experimental data for both mixers by a deviation within +/- 10%. Furthermore, the tube fitted with a 120.degrees-blades mixer yields higher thermal performance with a maximum value of 1.77. As well, the 120 degrees-blades mixer provides thermal performance factors up to 17% greater than that for 90 degrees-blades mixer for the same pumping power, which implies that heat transfer effects significantly dominate pressure drop effects.
引用
收藏
页数:9
相关论文
共 53 条
[21]   Multi objective optimization of vortex generators for heat transfer enhancement using large design space exploration [J].
Karkaba, H. ;
Dbouk, T. ;
Habchi, C. ;
Russeil, S. ;
Lemenand, T. ;
Bougeard, D. .
CHEMICAL ENGINEERING AND PROCESSING-PROCESS INTENSIFICATION, 2020, 154 (154)
[22]   Experimental investigation on heat transfer enhancement in a circular tube with equilateral triangle cross sectioned coiled-wire inserts [J].
Keklikcioglu, Orhan ;
Ozceyhan, Veysel .
APPLIED THERMAL ENGINEERING, 2018, 131 :686-695
[23]   Heat transfer enhancement and pressure drop by pulsating flow through helically coiled tube: An experimental study [J].
Khosravi-Bizhaem, Hamed ;
Abbassi, Abbas ;
Ravan, Amir Zivari .
APPLIED THERMAL ENGINEERING, 2019, 160
[24]   The cross-sectional curvature effect of twisted tapes on heat transfer performance [J].
Kosker, Muslume ;
Yilmaz, Fuat .
CHEMICAL ENGINEERING AND PROCESSING-PROCESS INTENSIFICATION, 2020, 154
[25]   Heat transfer enhancement of internal laminar flows using additively manufactured static mixers [J].
Kwon, Beomjin ;
Liebenberg, Leon ;
Jacobi, Anthony M. ;
King, William P. .
INTERNATIONAL JOURNAL OF HEAT AND MASS TRANSFER, 2019, 137 :292-300
[26]   Heat transfer and the continuous production of hydroxypropyl starch in a static mixer reactor [J].
Lammers, Gerard ;
Beenackers, Antonie A. C. M. .
CHEMICAL ENGINEERING SCIENCE, 1994, 49 (24B) :5097-5107
[27]   Heat transfer to Newtonian and non-Newtonian fluids flowing in a sulzer SMX static mixer [J].
Li, HZ ;
Fasol, C ;
Choplin, L .
CHEMICAL ENGINEERING COMMUNICATIONS, 1998, 170 :23-37
[28]   An experimental and numerical study on the laminar heat transfer and flow characteristics of a circular tube fitted with multiple conical strips inserts [J].
Liu, Peng ;
Zheng, Nianben ;
Shan, Feng ;
Liu, Zhichun ;
Liu, Wei .
INTERNATIONAL JOURNAL OF HEAT AND MASS TRANSFER, 2018, 117 :691-709
[29]   HEAT TRANSFER AND PRESSURE DROP IN TAPE-GENERATED SWIRL FLOW OF SINGLE-PHASE WATER [J].
LOPINA, RF ;
BERGLES, AE .
JOURNAL OF HEAT TRANSFER, 1969, 91 (03) :434-&
[30]  
Manglik R.M., 2003, Heat Transfer Handbook, P1029