Erratum to 'Conjugate heat/mass transfer from a circular cylinder with an internal heat/mass source in laminar crossflow at low Reynolds numbers' [Int. J. Heat Mass Transf. 48 (2005) 419-424] and 'Unsteady conjugate heat/mass transfer from a circular cylinder in laminar crossflow at low Reynolds numbers' [Int. J. Heat Mass Transf. 47 (2004) 2469-2480]

Gh. Juncu

首页> 外文期刊>International Journal of Heat and Mass Transfer >Erratum to 'Conjugate heat/mass transfer from a circular cylinder with an internal heat/mass source in laminar crossflow at low Reynolds numbers' [Int. J. Heat Mass Transf. 48 (2005) 419-424] and 'Unsteady conjugate heat/mass transfer from a circular cylinder in laminar crossflow at low Reynolds numbers' [Int. J. Heat Mass Transf. 47 (2004) 2469-2480]

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Erratum to 'Conjugate heat/mass transfer from a circular cylinder with an internal heat/mass source in laminar crossflow at low Reynolds numbers' [Int. J. Heat Mass Transf. 48 (2005) 419-424] and 'Unsteady conjugate heat/mass transfer from a circular cylinder in laminar crossflow at low Reynolds numbers' [Int. J. Heat Mass Transf. 47 (2004) 2469-2480]

机译：勘误“以低雷诺数在层流错流中结合来自带有内部热/质量源的圆柱体的热/质量传递” [Int。 J.热传质。 48（2005）419-424]和“在低雷诺数下，层流错流中圆柱的非稳态共轭热/质量传递” [Int。 J.热传质。 47（2004）2469-2480]

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The conjugate heat/mass transfer from a circular cylinder in laminar crossflow was analysed in [1,2]. Unfortunately, due to an error occurred during data processing, the figures that present in [1,2] the local Nu number are wrong.rnFig. 1 of the present note shows the accurate values of the local Nu number for the case analysed in [1]. Thermal wake exists only in the region of the rear stagnation point (θ = 0). For flow without separation (Re = 2 - Fig. la), the evolution of the thermal wake phenomenon is similar to that observed for spheres in creeping flow. For flow with separation (Re = 20 - Fig. lb) thermal wake occurs in the vicinity of the flow separation point. Thus, the discussions from [1] about the thermal wake phenomenon and the last column of Table 5 should be ignored. All the other results presented in [1], i.e. asymptotic values of the average Nu values (overall and fractional), time variation of the cylinder average temperature, the influence of kinetic and thermodynamic ratios on conjugate transfer, remain valid.

机译：在[1,2]中分析了层流错流中来自圆柱的共轭热/质量传递。不幸的是，由于在数据处理过程中发生了错误，因此[1,2]本地Nu编号中的数字是错误的。本说明的1显示了针对[1]中分析的案例的本地Nu数的准确值。热尾流仅存在于后停滞点（θ= 0）的区域。对于没有分离的流（Re = 2-图1a），热唤醒现象的演变与蠕变流中的球体所观察到的相似。对于分离的流（Re = 20-图lb），在流分离点附近会发生热唤醒。因此，应忽略[1]中有关热唤醒现象的讨论以及表5的最后一栏。 [1]中提出的所有其他结果，即平均Nu值（整体和分数）的渐近值，圆柱体平均温度的时间变化，动力学和热力学比对共轭转移的影响仍然有效。

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《International Journal of Heat and Mass Transfer》 |2008年第12期|3255-3257|共3页
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Gh. Juncu;
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收录信息美国《科学引文索引》(SCI);美国《工程索引》(EI);
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1. Conjugate heat/mass transfer from a circular cylinder with an internal heat/mass source in laminar crossflow at low Reynolds numbers [J] . Gh. Juncu International Journal of Heat and Mass Transfer . 2005,第2期

机译：在低雷诺数下以层流错流的方式结合来自带有内部热/质量源的圆柱体的热/质量传递
2. Unsteady conjugate heat/mass transfer from a circular cylinder in laminar crossflow at low Reynolds numbers [J] . Gh. Juncu International Journal of Heat and Mass Transfer . 2004,第10a11期

机译：低雷诺数下层流错流中圆柱体的非稳态共轭热/质量传递
3. Corrigendum to 'Experimental investigation on heat transfer in laminar, transitional and turbulent circular pipe flow' [Int. J. Heat Mass Transfer 95(2016)1008-1018] [J] . Bertsche Dirk, Knipper Paul, Wetzel Thomas International Journal of Heat and Mass Transfer . 2019,第OCTa期

机译：“层流，过渡和湍流圆管流中传热的实验研究”勘误[Int。 J.传质95（2016）1008-1018]
4. HEAT TRANSFER AND WAKE INTERACTION DYNAMICS FOR LOW MASS-DAMPING CYLINDER UNDERGOING FLOW-INDUCED VIBRATION AT HIGH REYNOLDS NUMBER [C] . Amr Elbanhawy, Ali Turan ASME Joint US-European Fluids Engineering Division summer meeting;FEDSM2010;International symposium on fluid-structure interactions, flow-sound interactions, and flow-induced vibration and noise . 2011

机译：高雷诺数下流动诱导的低阻尼气缸传热和尾流相互作用动力学
5. A THEORETICAL AND NUMERICAL INVESTIGATION OF LAMINAR BOUNDARY-LAYER HEAT AND MASS TRANSFER IN NATURAL CONVECTION: I. SIMULTANEOUS HEAT AND MASS TRANSFER. II. MASS TRANSFER IN THE ABSENCE OF HEAT TRANSFER [D] . CARDNER, DAVID VICTOR. 1963

机译：自然对流层流边界层传热和传质的理论和数值研究：I。同时传热和传质。二。没有传热时的传质
6. Effects of Lewis number on coupled heat and mass transfer in a circular tube subjected to external convective heating [O] . Anjun Jiao, Yuwen Zhang, Hongbin Ma, -1

机译：刘易斯数对外部对流加热圆管内传热传质的影响
7. Discussion: “Force Convection Heat Transfer at an Inclined and Yawed Square Plate—Application to Solar Collectors” (Sparrow, E. M., and Tien, K. K., 1977, ASME J. Heat Transfer, 99, pp. 507–512) and “Local Heat Transfer and Fluid Flow Characteristics for Airflow Oblique or Normal to Square Plate” (Tien, K. K., and Sparrow, E. M., 1979, Internation Journal of Heat and Mass Transfer, 22, pp. 349–359) and “Effect of Finite Width on Heat Transfer and Fluid Flow about an Inclined Rectangular Plate” (Sparrow, E. M., Ramsey, J. W., and Mass, E. A., 1979, ASME J. Heat Transfer, 101, pp. 199–204) [O] . B. Nimmo, S. Zubair 1981

机译：讨论：“在倾斜和偏航的方形板应用于太阳能收集器的强制对流传热”（Sparrow，EM和Tien，KK，1977，Asme J.传热，99，PP。507-512）和“局部热量用于气流倾斜或正常板的转移和流体流动特性“（Tien，KK和Sparrow，EM，1979，热量和传质杂志，22，pp.349-359）和”有限宽度对热量的影响关于倾斜矩形板的转移和流体流动“（Sparrow，EM，Ramsey，JW和Mass，EA，1979，ASME J.传热，101，PP。199-204）
8. Heat-Mass-Transfer-6. Vol. 4. Heat and Mass Transfer on Changing of Agregate State of Matter. Pt. 2. Heat and Mass Transfer on Phase Transitions and in Heat Tubes [R] . Seifert, H. 1980

机译：热传质-6。卷。 4.改变agregate物质状态的传热传质。铂。 2.相变和热管的传热传质

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