2015
DOI: 10.1016/j.ces.2015.06.009
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Heat transfer enhancement in three-start spirally corrugated tube: Experimental and numerical study

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Cited by 75 publications
(23 citation statements)
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“…The main research efforts over the last five years have been focused on investigating spirally or transversally corrugated tubes and channels, fins or inserts of wavy strip tapes, and other techniques that allow disturbance of thermal boundary layers [8][9][10][11][12][13][14][15][16]. A concept of fluted tubes was investigated by Srinivasan et al [12].…”
Section: Introductionmentioning
confidence: 99%
“…The main research efforts over the last five years have been focused on investigating spirally or transversally corrugated tubes and channels, fins or inserts of wavy strip tapes, and other techniques that allow disturbance of thermal boundary layers [8][9][10][11][12][13][14][15][16]. A concept of fluted tubes was investigated by Srinivasan et al [12].…”
Section: Introductionmentioning
confidence: 99%
“…Enhanced heat transfer in laminar flow in three-start spirally corrugated tubes was reported by Kareem et al. 13 Their results showed that the heat transfer enhancement, friction factor, and thermal performance of corrugated tubes were higher than those of a smooth tube in the ranges of 2.4–3.7, 1.7–2.4, and 1.8–3.4 higher, respectively. Eiamsa-ard et al.…”
Section: Introductionmentioning
confidence: 69%
“…Heat transfer improvement by single-start corrugated tubes was reported by many investigators. 118 In 1969, Kidd 1 investigated heat transfer and pressure drop of gas flow inside spirally corrugated tubes with groove depths of 0.003–0.028 in. He found that all the spirally corrugated tubes tested gave higher heat transfer than a smooth tube.…”
Section: Introductionmentioning
confidence: 99%
“…In the investigation, they proposed four models: one-start, two-start, three-start, and four-start spirally corrugated tubes in RBHXsSCT (rod-baffle heat exchangers with spirally corrugated tubes), and the results showed that when Reynolds number ranged from 6,000 to 18,000, compared with RBHX (rodbaffle heat exchangers with plain tubes), the heat transfer quantities were higher and the pressure drop was lower. Kareem et al [27] studied the heat transfer enhancement in a three-start spirally corrugated tube experimentally and numerically, and found that at low Reynolds number; the three-start spirally corrugated tube can improve the heat transfer significantly with a modest increase in the friction factor. Chen et al [28] conducted an experiment, focusing on the nonsymmetric nature of the corrugation angles along the longitudinal direction of four-start spirally corrugated tubes, and found that altering the internal non-symmetric wavy shapes of the tubes enabled to manipulation of the heat transfer and friction characteristics.…”
Section: Introductionmentioning
confidence: 99%