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Numerical investigation on condensation heat transfer and pressure drop characteristics of R134a in horizontal flattened tubes EI SCIE
期刊论文 | 2018 , 85 , 441-461 | INTERNATIONAL JOURNAL OF REFRIGERATION-REVUE INTERNATIONALE DU FROID
WoS CC Cited Count: 4
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Abstract :

The condensation performance of R134a in horizontal round tubes and flattened tubes was numerically investigated. Three round tubes with different hydraulic diameters (d(h) = 3.25, 4.57 and 6.5 mm) were deformed into flattened tubes with the aspect ratio (AR) equals to 2, 4 and 6, respectively. The liquid film thickness combined with the interface line was shown in detail to illustrate the effect of shear stress, surface tension and gravity. The heat transfer coefficients increased with the vapor quality and aspect ratio, and the enhancement was magnified at higher vapor quality and mass velocity. The smaller the original round tube diameter was, the higher the enhancement of thermal performance in flattened tubes was. The average film thickness of flattened tubes with AR = 2, 4, 6 was respectively 35%, 50% and 60% thinner than that of round tube. The relative role of surface tension and gravity determined the local thermal performance in flattened tubes. The main thermal resistance was located in the arc. The gravity effect was almost negligible in the straight part but still played an important role in the arc of flattened tubes. The heat exchanging process mainly occurred near the intersection of straight part and arc and this location tends to move toward the straight side for smaller flattened tubes because of the reinforcement of the surface tension effect. The pressure gradient also increased with the vapor quality, aspect ratio and mass velocity but decreased with the increasing hydraulic diameter. The existing correlations almost tend to underestimate both the heat transfer coefficients and pressure gradients. Two improved correlations of condensation heat transfer and pressure gradient in flattened tube were developed for practical applications. (C) 2017 Elsevier Ltd and IIR. All rights reserved.

Keyword :

Heat transfer coefficient Pressure gradient Condensation R134a Flattened tube

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GB/T 7714 Wen, Jian , Gu, Xin , Wang, Simin et al. Numerical investigation on condensation heat transfer and pressure drop characteristics of R134a in horizontal flattened tubes [J]. | INTERNATIONAL JOURNAL OF REFRIGERATION-REVUE INTERNATIONALE DU FROID , 2018 , 85 : 441-461 .
MLA Wen, Jian et al. "Numerical investigation on condensation heat transfer and pressure drop characteristics of R134a in horizontal flattened tubes" . | INTERNATIONAL JOURNAL OF REFRIGERATION-REVUE INTERNATIONALE DU FROID 85 (2018) : 441-461 .
APA Wen, Jian , Gu, Xin , Wang, Simin , Li, Yanzhong , Tu, Jiyuan . Numerical investigation on condensation heat transfer and pressure drop characteristics of R134a in horizontal flattened tubes . | INTERNATIONAL JOURNAL OF REFRIGERATION-REVUE INTERNATIONALE DU FROID , 2018 , 85 , 441-461 .
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On wall-normal motions of inertial spheroids in vertical turbulent channel flows EI SCIE Scopus
期刊论文 | 2018 , 229 (7) , 2947-2965 | ACTA MECHANICA
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Abstract :

Dynamics of inertial non-spherical particles in upward and downward turbulent channel flows are investigated. Oblate (disk-like) and prolate (rod-like) spheroids are considered in a Lagrangian point-particle approach in which the turbulence field is obtained by direct numerical simulations. Fluid and particle statistics are conditionally sampled with the view to distinguish between particles moving toward or away from the channel walls. Outward-moving particles tend to locate more in lower-speed streamwise fluid streaks than inward-moving particles. For highly inertial spheroids, these tendencies are differently affected by gravity in upward and downward flows. The gravity force is therefore believed to influence turbophoresis. The tendency of oblate and prolate spheroids to orient parallel with and normal to the spanwise direction near the walls is stronger for outward- than for inward-moving particles. These distinctions are ascribed to the wall-normal force on the spheroids from the surrounding fluid. In the absence of gravity, heavy spheroids in the channel center align randomly with the almost isotropic fluid vorticity. Gravity is seen to have a de-isotropization effect on the particles' orientation in the inertial frame.

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GB/T 7714 Yuan, Wenjun , Zhao, Lihao , Challabotla, Niranjan Reddy et al. On wall-normal motions of inertial spheroids in vertical turbulent channel flows [J]. | ACTA MECHANICA , 2018 , 229 (7) : 2947-2965 .
MLA Yuan, Wenjun et al. "On wall-normal motions of inertial spheroids in vertical turbulent channel flows" . | ACTA MECHANICA 229 . 7 (2018) : 2947-2965 .
APA Yuan, Wenjun , Zhao, Lihao , Challabotla, Niranjan Reddy , Andersson, Helge I. , Deng, Jianqiang . On wall-normal motions of inertial spheroids in vertical turbulent channel flows . | ACTA MECHANICA , 2018 , 229 (7) , 2947-2965 .
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The comparison of condensation heat transfer and frictional pressure drop of R1234ze(E), propane and R134a in a horizontal mini-channel EI SCIE
期刊论文 | 2018 , 92 , 208-224 | INTERNATIONAL JOURNAL OF REFRIGERATION-REVUE INTERNATIONALE DU FROID
WoS CC Cited Count: 1
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Abstract :

The steady-state condensation performance of R1234ze(E), propane and R134a in a horizontal circular mini-channel was numerically investigated. The effects of mass flux, vapor quality and physical properties on condensation performance were discussed. At the same condition, condensation heat performance of propane was the best and then the R134a and R1234ze(E). However, the pressure gradients of R1234ze(E) were larger than that of propane and R134a. The average film thickness of propane and R1234ze(E) were an average of 9.4% thicker and 15.7% thinner than that of R134a, respectively. The effective conductivity played an important role in the heat flow rate of three refrigerants. Unlike the R1234ze(E) and R134a for which the condensate tended to be stratified at x = 0.5, there was no obvious stratification for propane. The published correlations tended to underestimate the pressure gradients of R1234ze(E) significantly. (C) 2018 Elsevier Ltd and IIR. All rights reserved.

Keyword :

Condensation Mini-channel Propane R1234ze(E) Pressure gradient Heat transfer coefficient

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GB/T 7714 Wen, Jian , Gu, Xin , Wang, Simin et al. The comparison of condensation heat transfer and frictional pressure drop of R1234ze(E), propane and R134a in a horizontal mini-channel [J]. | INTERNATIONAL JOURNAL OF REFRIGERATION-REVUE INTERNATIONALE DU FROID , 2018 , 92 : 208-224 .
MLA Wen, Jian et al. "The comparison of condensation heat transfer and frictional pressure drop of R1234ze(E), propane and R134a in a horizontal mini-channel" . | INTERNATIONAL JOURNAL OF REFRIGERATION-REVUE INTERNATIONALE DU FROID 92 (2018) : 208-224 .
APA Wen, Jian , Gu, Xin , Wang, Simin , Li, Yanzhong , Tu, Jiyuan . The comparison of condensation heat transfer and frictional pressure drop of R1234ze(E), propane and R134a in a horizontal mini-channel . | INTERNATIONAL JOURNAL OF REFRIGERATION-REVUE INTERNATIONALE DU FROID , 2018 , 92 , 208-224 .
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Effect of surface tension, gravity and turbulence on condensation patterns of R1234ze(E) in horizontal mini/macro-channels EI SCIE Scopus
期刊论文 | 2018 , 125 , 153-170 | INTERNATIONAL JOURNAL OF HEAT AND MASS TRANSFER
WoS CC Cited Count: 1
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Abstract :

The condensation patterns of R1234ze(E) in circular mini/macro-channels with diameters ranged from 0.493 to 4.57 mm was numerically investigated. The effects of mass flux, vapor quality and tube diameter on heat transfer coefficients were analyzed. The relative role of surface tension, gravity and shear stress in mini/macro-channels was explored and the turbulence effect of liquid phase was discussed. The heat transfer coefficients increased with the mass flux, vapor quality and the decrease of tube diameter. The liquid film thickness decreased significantly when reducing the tube dimension for the increased shear stress. The surface tension was found to play a role to increase the heat performance by enhancing the heat convection between liquid film and wall surface, which was only obvious in mini-channels. Contrary to the effect of surface tension, the gravity effect was negligible in mini-channels with a diameter less than 1 mm, while had an important effect on heat transfer coefficients for macro-channels. The gravity affected both liquid film distribution and velocity field, which can either enhance or weaken the heat transfer coefficient during condensation flow. The turbulence in liquid film played an important role in reducing the local thermal resistance and was more important in tubes with larger diameter. The onset of turbulence inside the liquid film may occur at much lower liquid Reynolds numbers for mini-channels. (C) 2018 Elsevier Ltd. All rights reserved.

Keyword :

Mini/macro-channels Condensation Shear stress Surface tension Gravity Turbulence

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GB/T 7714 Wen, Jian , Gu, Xin , Liu, Yuce et al. Effect of surface tension, gravity and turbulence on condensation patterns of R1234ze(E) in horizontal mini/macro-channels [J]. | INTERNATIONAL JOURNAL OF HEAT AND MASS TRANSFER , 2018 , 125 : 153-170 .
MLA Wen, Jian et al. "Effect of surface tension, gravity and turbulence on condensation patterns of R1234ze(E) in horizontal mini/macro-channels" . | INTERNATIONAL JOURNAL OF HEAT AND MASS TRANSFER 125 (2018) : 153-170 .
APA Wen, Jian , Gu, Xin , Liu, Yuce , Wang, Simin , Li, Yanzhong . Effect of surface tension, gravity and turbulence on condensation patterns of R1234ze(E) in horizontal mini/macro-channels . | INTERNATIONAL JOURNAL OF HEAT AND MASS TRANSFER , 2018 , 125 , 153-170 .
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Thermal design and optimization of plate-fin heat exchangers based global sensitivity analysis and NSGA-II EI SCIE Scopus
期刊论文 | 2018 , 136 , 444-453 | APPLIED THERMAL ENGINEERING
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Abstract :

Morris and Sobol global sensitivity analyses are firstly studied to evaluate the effects of the design parameters on the performance of plate-fin heat exchanger with serrated fins. Five design parameters such as the fin height, fin space, fin thickness and interrupted length and channel Reynolds number are selected as optimization parameters. Heat flow rate, total annual cost and entropy generation number are considered as objective functions. Furthermore, the five design parameters are optimized by NSGA-II, in which the effectiveness of the proposed algorithm is validated by comparing a previous approach. The results show that Reynolds number and fin space s play a dominant role on the performance of plate-fin heat exchanger with serrated fin. Meanwhile, the interaction effects among these parameters are significant on total annual cost and entropy generation number. Compared with one common design, the thermal performance factor of another common design and two optimal parameters increases 8.4%, 41.2% and 58.4%, respectively. Combining global sensitivity analysis and NSGA-II has the characteristics of easy to implement and high accuracy. Therefore, it is universal and can be used for various complex engineering applications to provide guidance for better selecting the suitable parameters.

Keyword :

Morris method Genetic algorithm Sobol method Sensitivity analysis Serrated fin Plate-fin heat exchanger

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GB/T 7714 Yang, Huizhu , Wen, Jian , Wang, Simin et al. Thermal design and optimization of plate-fin heat exchangers based global sensitivity analysis and NSGA-II [J]. | APPLIED THERMAL ENGINEERING , 2018 , 136 : 444-453 .
MLA Yang, Huizhu et al. "Thermal design and optimization of plate-fin heat exchangers based global sensitivity analysis and NSGA-II" . | APPLIED THERMAL ENGINEERING 136 (2018) : 444-453 .
APA Yang, Huizhu , Wen, Jian , Wang, Simin , Li, Yanzhong . Thermal design and optimization of plate-fin heat exchangers based global sensitivity analysis and NSGA-II . | APPLIED THERMAL ENGINEERING , 2018 , 136 , 444-453 .
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Condensation flow patterns and model assessment for R1234ze(E) in horizontal mini/macro-channels EI Scopus
期刊论文 | 2018 , 134 , 140-159 | International Journal of Thermal Sciences
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Abstract :

Knowledge regarding the condensation flow patterns of environment friendly refrigerant R1234ze(E) in mini/macro-channels was important for alternative industrial applications. In this paper, the condensation heat transfer and pressure drop characteristic of R1234ze(E) in horizontal circular channels with diameter ranged from 0.493 to 4.57 mm were numerically investigated and compared with that of R134a. The detailed liquid film distribution, local film thickness and velocity field were presented for better understanding the condensation process. Both the heat transfer coefficients and pressure gradients increased with the mass flux, vapor quality and the decrease of the tube diameter. The heat transfer coefficients of R1234ze(E) were smaller than that of R134a, but the pressure gradients of R1234ze(E) were larger than that of R134a. The difference in heat transfer and pressure drop performance was found to be smaller in macro-channels. The effects of surface tension and gravity on liquid film distribution are significantly influenced by the tube diameter. The liquid film distribution was very close for R1234ze(E) and R134a for their similar physical properties. The average film thickness of R1234ze(E) was thinner than that of R134a. The axial velocity of the vapor phase decreased with the vapor quality, while the variation of the liquid phase velocity was associated with the circumferential position for the gravity effect. The simulated heat transfer coefficients and pressure gradients were compared with predicted values from the available well-known correlations. A new pressure drop correlation was proposed for practical application. © 2018 Elsevier Masson SAS

Keyword :

Condensation heat transfer Condensation process Environment friendly Heat transfer and pressure drop Local film thickness Mini/macro-channels Pressure drop correlation R1234ze

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GB/T 7714 Gu, Xin , Wen, Jian , Wang, Chunlong et al. Condensation flow patterns and model assessment for R1234ze(E) in horizontal mini/macro-channels [J]. | International Journal of Thermal Sciences , 2018 , 134 : 140-159 .
MLA Gu, Xin et al. "Condensation flow patterns and model assessment for R1234ze(E) in horizontal mini/macro-channels" . | International Journal of Thermal Sciences 134 (2018) : 140-159 .
APA Gu, Xin , Wen, Jian , Wang, Chunlong , Zhang, Xing , Wang, Simin , Tu, Jiyuan . Condensation flow patterns and model assessment for R1234ze(E) in horizontal mini/macro-channels . | International Journal of Thermal Sciences , 2018 , 134 , 140-159 .
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Effect of fin types and Prandtl number on performance of plate-fin heat exchanger: Experimental and numerical assessment EI Scopus
期刊论文 | 2018 , 144 , 726-735 | Applied Thermal Engineering
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Abstract :

An experimental investigation is performed using liquid R113 to study the thermohydraulic characteristics of plate-fin heat exchanger with plain, serrated and perforated fins. Meanwhile, three performance evaluation criteria j/f, j/f1/2 and j/f1/3 are used to qualitative compare their comprehensive performance. Further, to study the effects of heating condition and Prandtl number on heat transfer, a numerical model of serrated fins is carried out. The fin channels with a uniform heat flux at bottom end or at both bottom and upper ends are studied as two types of heating conditions, namely, single-fold and two-fold modes. Besides, using air (Pr = 0.744), R113 (Pr = 9.02) and ethylene glycol (Pr = 51.65) aqueous solution as working media, the Prandtl number effect is discussed. The results reveal that the comprehensive performance of serrated fins is the best. Colburn factor j of single-fold mode is lower than that of two-fold mode. The Colburn factor j decreases as the Prandtl number increases in laminar flow and it is independent of Prandtl number in turbulent flow. A modified Colburn factor j based on the Manglik & Bergles correlation is proposed as functions of (Pr/Prair)−0.04827 in laminar flow. The conclusions provide the guidance on the design of plate fin heat exchanger. © 2018 Elsevier Ltd

Keyword :

Comprehensive performance Experimental investigations Experimental study Fin geometry Fold mode Heating conditions Performance evaluation criteria Plate-fin heat exchanger

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GB/T 7714 Yang, Huizhu , Wen, Jian , Wang, Simin et al. Effect of fin types and Prandtl number on performance of plate-fin heat exchanger: Experimental and numerical assessment [J]. | Applied Thermal Engineering , 2018 , 144 : 726-735 .
MLA Yang, Huizhu et al. "Effect of fin types and Prandtl number on performance of plate-fin heat exchanger: Experimental and numerical assessment" . | Applied Thermal Engineering 144 (2018) : 726-735 .
APA Yang, Huizhu , Wen, Jian , Wang, Simin , Li, Yanzhong . Effect of fin types and Prandtl number on performance of plate-fin heat exchanger: Experimental and numerical assessment . | Applied Thermal Engineering , 2018 , 144 , 726-735 .
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Optimization investigation on configuration parameters of serrated fin in plate-fin heat exchanger based on fluid structure interaction analysis EI SCIE Scopus
期刊论文 | 2018 , 119 , 282-294 | INTERNATIONAL JOURNAL OF HEAT AND MASS TRANSFER
WoS CC Cited Count: 1 SCOPUS Cited Count: 1
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Abstract :

The comprehensive performance of serrated fin in plate-fin heat exchangers (PFHEs) is numerically studied based on fluid structure interaction (FSI) analysis in this paper. Based on Full 2nd-Order Polynomial response surface (RS) and analysis of variance (ANOVA), the effects and second order interaction effects of the fin height, fin space, fin thickness and fin interrupted length on heat transfer, flow resistance and stress are quantitatively and thoroughly assessed. The results show that the heat transfer is the most sensitive to fin interrupted length, and the flow resistance and the maximum stress are the most sensitive to fin thickness. The interaction effect of the fin space and fin interrupted length is the strongest when the j factor is set as objective function, while the interaction effect of the fin space and fin thickness is the strongest when the f factor or maximum stress is set as objective function. Based on Full 2nd-Order Polynomial RS, Multi-Objective Genetic Algorithm (MOGA) is applied to optimize the fin structure comprehensively, with enhancing heat transfer, decreasing pressure drop and stress set as objectives. To demonstrate the effectiveness of optimized structures, a comprasion between the original design and optimized structures is performed. The results show that the JF factor of optimized structures 2 and 3 increases by 23.0% and 19.7% respectively, and the maximum stress decreases by 5.8% and 15.2% respectively. The MOGA offers theorectical guidance for optimization design of PFHE. (C) 2017 Elsevier Ltd. All rights reserved.

Keyword :

Stress analysis Serrated fin Plate-fin heat exchanger Analysis of variance Response surface Multi-Objective Genetic Algorithm

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GB/T 7714 Wen, Jian , Li, Ke , Zhang, Xing et al. Optimization investigation on configuration parameters of serrated fin in plate-fin heat exchanger based on fluid structure interaction analysis [J]. | INTERNATIONAL JOURNAL OF HEAT AND MASS TRANSFER , 2018 , 119 : 282-294 .
MLA Wen, Jian et al. "Optimization investigation on configuration parameters of serrated fin in plate-fin heat exchanger based on fluid structure interaction analysis" . | INTERNATIONAL JOURNAL OF HEAT AND MASS TRANSFER 119 (2018) : 282-294 .
APA Wen, Jian , Li, Ke , Zhang, Xing , Wang, Chunlong , Wang, Simin , Tu, Jiyuan . Optimization investigation on configuration parameters of serrated fin in plate-fin heat exchanger based on fluid structure interaction analysis . | INTERNATIONAL JOURNAL OF HEAT AND MASS TRANSFER , 2018 , 119 , 282-294 .
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PIV experimental investigation on shell-side flow patterns of shell and tube heat exchanger with different helical baffles EI SCIE Scopus
期刊论文 | 2017 , 104 , 247-259 | INTERNATIONAL JOURNAL OF HEAT AND MASS TRANSFER | IF: 3.891
WoS CC Cited Count: 9
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Abstract :

Shell-side flow patterns in shell and tube heat exchanger with helical baffles (STHXsHB) have been experimentally investigated by particle image velocimetry (Ply), in which a series of velocity vector graphs are obtained in three typical cross-sections. Compared with the original heat exchanger with plain baffles, the flushing angle a of improved heat exchanger with fold baffles reduces in cross-section A and B, which is beneficial to heat transfer enhancement according to field synergy principle. Moreover, the vortex vanishes and the circumfluence obviously decreases in the cross-section C. The axial velocity u significantly decreases and the radial velocity v increases at the external of tube bundle because the external triangle leakage flows are blocked after the configuration improvement of baffles. The local pressure drops under the same distance in the middle part of tube bundles are basically the same in both original and improved heat exchangers. It illustrates that the flow patterns in shell side have an obvious periodicity. The further heat transfer experiments show that the integrative performance of the improved heat exchanger is enhanced by 2-8% under the identical operation conditions, which can be well explained by the results of PIV experiments where the field synergy angle alpha of velocity and heat flow fields is smaller in the improved heat exchanger. Therefore, this study is of great significance to help understand and analyze the reasons for the heat transfer enhancement of STHXs with fold baffles. (C) 2016 Elsevier Ltd. All rights reserved.

Keyword :

Helical baffles Shell and tube heat exchanger Triangular leakage zone Fold baffle PIV

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GB/T 7714 Wen, Jian , Yang, Huizhu , Wang, Simin et al. PIV experimental investigation on shell-side flow patterns of shell and tube heat exchanger with different helical baffles [J]. | INTERNATIONAL JOURNAL OF HEAT AND MASS TRANSFER , 2017 , 104 : 247-259 .
MLA Wen, Jian et al. "PIV experimental investigation on shell-side flow patterns of shell and tube heat exchanger with different helical baffles" . | INTERNATIONAL JOURNAL OF HEAT AND MASS TRANSFER 104 (2017) : 247-259 .
APA Wen, Jian , Yang, Huizhu , Wang, Simin , Gu, Xin . PIV experimental investigation on shell-side flow patterns of shell and tube heat exchanger with different helical baffles . | INTERNATIONAL JOURNAL OF HEAT AND MASS TRANSFER , 2017 , 104 , 247-259 .
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Sobol sensitivity analysis for governing variables in design of a plate-fin heat exchanger with serrated fins EI SCIE Scopus
期刊论文 | 2017 , 115 , 871-881 | INTERNATIONAL JOURNAL OF HEAT AND MASS TRANSFER | IF: 3.891
WoS CC Cited Count: 1
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Abstract :

Sobol sensitivity analysis can quantify the impact of input parameters' variations on the performance of plate-fin heat exchanger to guide the selection of input variables during design procedure. In this paper, the Reynolds number Re, fin height h, fin space s, fin thickness t and interrupted length I are considered as five input parameters, while exchanger volume, exchanger material content, heat flow rate and pressure drop with different constraints are taken as the design objectives. Moreover, to study the impact of Brandt number on input parameters, the Sobol sensitivity indices of five parameters are compared for air and water. The results show that the Reynolds number Re and fin spaces are the two main factors that affect the performance of plate fin heat exchanger. As the heat exchanger size limited, a smaller fin thickness t is selectable. Compared with air, the interrupted length l should be selected a smaller value for water. Guidance about the fin surface selection is given. Sobol sensitivity analysis methods can be performed to detect the importance of parameters in various complex engineering applications. And compared with other optimization algorithms, this method is simple to implement. (C) 2017 Elsevier Ltd. All rights reserved.

Keyword :

Sobol method Plate-fin heat exchanger Serrated fin Design optimization Sensitivity analysis

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GB/T 7714 Yang, Huizhu , Wen, Jian , Wang, Simin et al. Sobol sensitivity analysis for governing variables in design of a plate-fin heat exchanger with serrated fins [J]. | INTERNATIONAL JOURNAL OF HEAT AND MASS TRANSFER , 2017 , 115 : 871-881 .
MLA Yang, Huizhu et al. "Sobol sensitivity analysis for governing variables in design of a plate-fin heat exchanger with serrated fins" . | INTERNATIONAL JOURNAL OF HEAT AND MASS TRANSFER 115 (2017) : 871-881 .
APA Yang, Huizhu , Wen, Jian , Wang, Simin , Li, Yanzhong , Tu, Jiyuan , Cai, Wenjian . Sobol sensitivity analysis for governing variables in design of a plate-fin heat exchanger with serrated fins . | INTERNATIONAL JOURNAL OF HEAT AND MASS TRANSFER , 2017 , 115 , 871-881 .
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