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壳程多通道管壳式换热器中并列分置管束长宽比与深度换热 被引量:2

Ratio of length to width and deep heat transfer in multi-parallel-channel shell-and-tube heat exchangers
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摘要 为研究壳程多通道管壳式换热器中并列分置管束长宽比锐减对其内部速度场及深度换热性能的影响,抽取具有代表性的单元流路区域建立并列分置管束模型。对长宽比范围在1.85~9.23、传热管数目分别为10,20,30,40和50的5个并列分置管束模型应用FLUENT软件进行了数值模拟。研究结果表明:当管程与壳程轴流段平均速度均为10 m/s时,随长宽比锐减,并列分置管束换热性能下降且壳程阻力显著增加,壳程流体速度分布越来越不均匀。在典型工况下,长宽比大于4.62的并列分置管束中冷流体出口温度高于热流体出口温度,即可以实现深度换热,在长宽比小于3.08的并列分置管束模型中不能实现深度换热。这为壳程多通道管壳式换热器的结构设计提供参考依据。 In order to investigate the effect of ratio of length to width(L/W) decrease on velocity distributions and deep heat transfer performances in tube bundles in multi-parallel-channel(MPC) shell-and-tube heat exchangers(STHXs),tube bundle model was formulated based on a classical flow channel unit.Numerical investigation was carried out for five tube bundle models with tube numbers of 10,20,30,40 and 50 for L/W ranging from 1.85 to 9.23,respectively.The computations were carried out using FLUENT,a commercial CFD code.The simulation results show that when axial average velocity is 10 m/s both in the shell side and the tube side,outlet temperature of cold air is bigger than that of hot one,that is,deep heat transfer performance can be achieved in tube bundles with L/W bigger than 4.62,and deep heat transfer performance can not be achieved in tube bundles with L/W smaller than 3.08.A powerful reference for optimal design of multi-parallel-channel STHXs is provided by the results.
出处 《中南大学学报(自然科学版)》 EI CAS CSCD 北大核心 2011年第11期3564-3571,共8页 Journal of Central South University:Science and Technology
基金 国家自然科学基金资助项目(20776046)
关键词 计算流体动力学 深度换热 数值分析 长宽比 computational fluid dynamic deep heat transfer numerical analysis ratio of length to width
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  • 1徐景霞.新世纪石油化工装备技术发展初探[J].石油化工设备,2000,29(1):1-3. 被引量:1
  • 2王廷俊.化学工业装备技术发展趋势[J].化工管理,2004(2):24-25. 被引量:3
  • 3王颖.大型硫酸装置国产化工艺和设备[J].硫酸工业,2005(6):4-12. 被引量:5
  • 4Santacesaria E, Di Serio M, Tesser R, et al. Use of a corrugated plates heat exchanger reactor for obtaining biodiesel with very high productivity[J]. Energy & Fuels, 2009, 23(10): 5206-5212. 被引量:1
  • 5TIAN Li-ting, HE Ya-ling, TAO Yu-bing, et al. A comparative study on the air-side performance of wavy fin-and-tube heat exchanger with punched delta winglets in staggered and in-line arrangements[J]. International Journal of Thermal Sciences, 2009, 48(9): 1765-1776. 被引量:1
  • 6Ismail L S, Ranganayakulu C, Shah R K. Numerical study of flow patterns of compact plate-fin heat exchangers and generation of design data for offset and wavy fins[J]. International Journal of Heat and Mass Transfer, 2009, 52(17/18) 3972-3983. 被引量:1
  • 7TANG Gang-zhi, LI Long-jian, CUI Wen-zhi, et al. Experimental research on heat transfer characteristics of fined pipe heat exchanger with latent heat storage[J]. Journal of Zhengzhou University: Engineering Science, 2008, 29(3): 69-72. 被引量:1
  • 8Mandal M M, Nigam K D E Experimental study on pressure drop and heat transfer of turbulent flow in tube in tube helical heat exchanger[J]. Industrial & Engineering Chemistry Research, 2009, 48(20): 9318-9324. 被引量:1
  • 9Taymaz I, Koc I, Islamoglu Y. Experimental study on forced convection heat transfer characteristics in a converging diverging heat exchanger channel[J]. Heat and Mass Transfer, 2008, 44(10) 1257-1262. 被引量:1
  • 10王杨君,邓先和,李志武,洪蒙纳.旋流片支撑管束的传热与流阻性能[J].化工学报,2007,58(1):21-26. 被引量:13

二级参考文献28

共引文献23

同被引文献23

  • 1解增忠,张俊峰,罗雄麟,陈育昆,季德伟.管壳换热器模型库及在换热网络仿真中的应用[J].系统仿真学报,2005,17(12):2882-2887. 被引量:15
  • 2方骁,蒋柱武,张亚雷,杨海真.厌氧颗粒污泥性质与颗粒化研究新进展[J].江苏环境科技,2005,18(4):44-46. 被引量:7
  • 3董其伍,刘敏珊,赵晓冬.杆栅支撑纵流壳程换热器壳侧流体流动与传热的数值模拟[J].化工学报,2006,57(5):1073-1078. 被引量:22
  • 4孙宝芝,曹民侠,赵嘉明,李彦军.管壳式换热器瞬态换热性能分析[J].哈尔滨工程大学学报,2007,28(12):1332-1336. 被引量:5
  • 5Lutcha 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
  • 6Stehlik P, Nemcansky J, Kral D. Comparison of correction factors for shell-and-tube heat exchangers with segmental or helical baffles[J]. Heat Transfer Engineering, 1994, 15(1): 55-65. 被引量:1
  • 7Kral D, Stelik P, Van Der Ploeg H J, et aL Helical baffles in shell-and-tabe heat exchangers, part one: Experimental verification[J]. Heat Transfer Engineering, 1996, 17(1): 93-101. 被引量:1
  • 8ZHANG Jianfei, HE Yaling, TAO Wenquan. 3D numerical simulation on shell-and-tube heat exchangers with middle-overlapped helical baffles and continuous baffles. Part I: Numerical model and results of whole heat exchanger with middle-overlapped helical baffles[J]. International Journal of Heat and Mass Transfer, 2009, 52(23/24): 5371-5380. 被引量:1
  • 9ZHANG Jianfei, HE Yaling, TAO Wenquan. 3D numerical simulation on shell-and-tube heat exchangers with middle-overlapped helical baffles and continuous baffles. Part II: Simulation results of periodic model and comparison between continuous and noncontinuous helical baffles[J]. International Journal of Heat and Mass Transfer, 2009, 52(23/24): 5381-5389. 被引量:1
  • 10Farhad N T, Sirous Z M, Kazem R, et al. Baffle space impact on the performance of helical baffle shell and tube heat exchangers[J]. Applied Thermal Engineering, 2012, 44: 143-149. 被引量:1

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