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Effects of Shape and Quantity of Helical Baffle on the Shell-side Heat Transfer and Flow Performance of Heat Exchangers 被引量:6

螺旋折流板形状和数量对换热器壳侧传热及流动特性的影响(英文)
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摘要 Shape and quantity of helical baffles have great impact on the shell-side performance of helical baffled heat exchangers (HBHE). In this work, three physical models of HBHE with baffles of different shape (trisection, quadrant and sextant sector) were investigated. Numerical simulations were performed on HBHE at three helix an- gles (10°, 25° and 40°) by the software ANSYS CFX. Analyses of numerical results indicate that the sextant HBHE shows relatively better fluid flow performance because the leakage flow in the triangle area is evidently reduced and the fluid streamline appears much closer to an ideal spiral flow, while the trisection and quadrant HBHE show more scattered and disordered streamline distributions. The convective heat transfer coefficient and pressure drop in three types of HBHE were presented. Further investigations on the shell side performance with different helical baf- fles were implemented by the field synergy theory. Both theoretical and numerical analyses gave support on the re- lations between helical baffle shape and shell-side performance. This paper may provide useful reference for the selection of baffle shade and auantitv in HBHE. Shape and quantity of helical baffles have great impact on the shell-side performance of helical baffled heat exchangers(HBHE). In this work, three physical models of HBHE with baffles of different shape(trisection, quadrant and sextant sector) were investigated. Numerical simulations were performed on HBHE at three helix angles(10°, 25° and 40°) by the software ANSYS CFX. Analyses of numerical results indicate that the sextant HBHE shows relatively better fluid flow performance because the leakage flow in the triangle area is evidently reduced and the fluid streamline appears much closer to an ideal spiral flow, while the trisection and quadrant HBHE show more scattered and disordered streamline distributions. The convective heat transfer coefficient and pressure drop in three types of HBHE were presented. Further investigations on the shell side performance with different helical baffles were implemented by the field synergy theory. Both theoretical and numerical analyses gave support on the relations between helical baffle shape and shell-side performance. This paper may provide useful reference for the selection of baffle shape and quantity in HBHE.
出处 《Chinese Journal of Chemical Engineering》 SCIE EI CAS CSCD 2014年第3期243-251,共9页 中国化学工程学报(英文版)
基金 Supported by the National Natural Science Foundation of China(51106090) the National Key Basic Research Program of China(2013CB228305) the Independent Innovation Foundation of Shandong University(2012TS190)
关键词 helical baffled heat exchanger trisection QUADRANT SEXTANT field synergy principle 螺旋折流板换热器 流动特性 壳侧 流动性能 传热 外形 数值分析 ANSYS
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  • 1王秋旺.螺旋折流板管壳式换热器壳程传热强化研究进展[J].西安交通大学学报,2004,38(9):881-886. 被引量:82
  • 2Guo Z Y, Li D Y, Wang B X. A Novel Concept for Convective Heat Transfer Enhancement. International Journal of Heat and Mass Transfer, 1998, 41:2221-2225. 被引量:1
  • 3Tao W Q, He Y L, Wang Q W, et al. A Unified Analysis on Enhancing Single Phase Convective Heat Transfer with Field Synergy Principle. International Journal of Heat and Mass Transfer, 2002, 45:4871-4879. 被引量:1
  • 4Lutcha J, Nemcansky J. Performance Improvement of Tubular Heat Exchangers by Helical Baffles [J]. Chemi- cal Engineering Research &: Design, 1990, 68(3): 263-270. 被引量:1
  • 5Stehlik P, Nemcansky J, Kral D, et al. Comparison of Correction Factors for Shell-and-Tube Heat Exchangers With Segmental or Helical Baffles [J]. Heat Transfer En- gineering, 1994, 15(1): 55-65. 被引量:1
  • 6Stehlik P, Wadekar V. Different Strategies to Improve In- dustrial Heat Exchange [J]. Heat Transfer Engineering, 2002, 23(6): 36 -48. 被引量:1
  • 7Andrews M, Master B I. Three-Dimensional Modelling of a Helixchanger Heat Exchanger Using CFD [J]. Heat Transfer Engineering, 2005, 26(6): 22-31. 被引量:1
  • 8Master B I, Chunangad K S, Boxma A J, et al. Most Fre- quently Used Heat Exchangers From Pioneering Research to Worldwide Applications [J]. Heat Transfer Engineering, 2006, 27(6): 4- 11. 被引量:1
  • 9Lutcha J, Nemcansky J. Performance improvement of tubular heat exchangers by helical baffles[J]. Chemical Engineering Research& Design, 1990, 68 (3) : 263-270. 被引量:1
  • 10Stehlik Petr, Vishwas V, Wadekar. Different strategies to improve industrial heat exchanger [J]. Heat Transfer Engineering, 2002, 23 (6):36. 被引量:1

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