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IRJET- Heat Transfer Enhancement with Flag Vortex Generator
1.
International Research Journal
of Engineering and Technology (IRJET) e-ISSN: 2395-0056 Volume: 06 Issue: 07 | July 2019 www.irjet.net p-ISSN: 2395-0072 © 2019, IRJET | Impact Factor value: 7.211 | ISO 9001:2008 Certified Journal | Page 2009 Heat Transfer Enhancement with Flag Vortex Generator Mr. Anil V. Fajage1, Dr. Kiran More2, Prof. Avinash Patil3 1Mech. Dept. (Heat Power), Savitribai Phule Pune University, DYPIET, Ambi, Pune. 2Mech Dept., Dr. D. Y. Patil Insti .Of Engg., Ambi, Pune, INDIA. 3Mech Dept., Dr. D. Y. Patil School of Engg. Academy, Ambi, Pune, INDIA. ---------------------------------------------------------------------***---------------------------------------------------------------------- Abstract - The use of flexible plates or “flags” as vortex Creators inside a duct was successfully demonstrated as an one moreheat transfer enhancement method. There is a need to conduct further investigations on this technique to fully establish its thermal characteristics. A review of existing literature revealed that the abundance of investigations concerningthedynamicsof flagswas not complemented by the existing reports on the thermal characteristics of flag vortex generators. The Maximum of studies are Analytical in nature, the need to conduct experimental Study. The same can be said for the thermal performance of flag vortex generators. There are no intensive and extensive investigations on the thermal characteristics of flags vortex generator. CFD simulation of rigid flag significantly improved the thermal efficiency than smooth plate. The effects of channel height, and Reynolds number on the thermal efficiency will observe, and an optimal parameter set will be used. Experimental heat transfer over a flat plate and with Flag as vortex generated will be conducted. Key Words: Flag, Heat Transfer, Vortex Generator, Duct, Enhancement etc. 1. INTRODUCTION This the various techniques are used to enhance the rate of heat transfer over surface of plate. It may be passive or active technique. The significant pressure drags produced by the rib or pin fin protrusion into the flow. Heat transfer inside flow inside the duct can be enhanced by using passive surface modifications such as rib tabulators, protrusions, pin fins, Extended Surfaces and dimples. This heat transfer improvement methods have practical application for internal cooling of turbine aerofoils, combustion chambers liners and electronics cooling devices, biomedical devicesandheatexchangers.Theheattransfercanbeincreasedby the following different Augmentation Techniques. They are broadly classified into three different categories: I. Passive Techniques II. Active Techniques III. Compound Techniques. 1.1 Vortex heat transfer enhancement technique: Each Flags acts as a “Vortex Generator” which provides an intensiveandstableheatand masstransfer betweenthesurface and gaseous heating/cooling media. Taking advantages of VHTE, as a) higher heat transfer coefficient b) negligible pressure drop penalty c) potential from fouling rate reduction d) simplicity in design and fabrication e) compactness and/or lower cost. This method is more useful in heat transferenhancement inconvectivepassagesforindustrial boilers,processheatersand furnaces and heat exchangers variety forotherindustrieslikeautomotive(radiators,oilcoolersetc.),heattreating(recuperates etc.), power electronics (convective coolers etc.), aerospace, military, food processors etc. 1.2 Problem Statement: Experimental Investigation of Heat Transfer Enhancement with Inline andStaggeredFlagasVortexGeneratorandneedto compare with Flat Plate.
2.
International Research Journal
of Engineering and Technology (IRJET) e-ISSN: 2395-0056 Volume: 06 Issue: 07 | July 2019 www.irjet.net p-ISSN: 2395-0072 © 2019, IRJET | Impact Factor value: 7.211 | ISO 9001:2008 Certified Journal | Page 2010 1.3 Objectives: I. Investigation of Heat transfer enhancement in Flag as Vortex Generator. II. Pressure drop estimation in Flag Vortex Generator. III. To enhance the heat transfer augmentation with minimum pressure, drop. IV. Thermal Performance enhancement analysis in Flag Vortex Generator. V. To get experimental results and CFD results for align arrangement of inline and staggered flags comparing with smooth flat plate. VI. Experimentation of smooth flat plate, inline flags and staggered flags are carried out for air velocity ranges from 0.5m/s to 2.5m/s. VII. Will propose best geometry and best arrangement which gives maximum Thermal Performance. 1.4 Flow Parameters: Reynold’s Number: The Reynolds number associated with the flow can be calculated by using following mathematical equation. …….. (1) Where, ρ is the density of the fluid in Kg/m3 V is the velocity of the fluid in _m/s Dh is hydraulic diameter in mm µ is the viscosity of the fluid in Ns/ m The hydraulic diameter Dh is calculated by using mathematical relation, Dh=2(W*H)/(W+H) …….. (2) Where, W= width of duct and H = height of Duct. Pressure drop penalty is calculated by taking the ratio of Pressure drop of modified flag i.e. inline flags and staggered flags to Pressure drop of smooth flat plate. …….. (3) 1.5 Geometric Parameters: Test Channel: The material for test channel is Aluminum. Table 1. Test section and channel Dimensions. Sr. No. Parameter Dimensions 1 Length of test channel (L) 150mm 2 Width at test channel (W) 150mm 3 Thickness of test channel (t) 15mm 4 Length of duct 1m 5 Height of Duct (h) 100mm
3.
International Research Journal
of Engineering and Technology (IRJET) e-ISSN: 2395-0056 Volume: 06 Issue: 07 | July 2019 www.irjet.net p-ISSN: 2395-0072 © 2019, IRJET | Impact Factor value: 7.211 | ISO 9001:2008 Certified Journal | Page 2011 1.6 Calculation Steps: 1. Heat absorbed by air: Q = mcp ΔT …… (4) Where, m is mass flow rate of air cp is heat carrying capacity rate of air ΔT is change in temperature of air (To- Ti) 2. Heat transfer by convection Q= hA ΔT …….. (5) Where, h is heat transfer coefficient of air A is surface area of test plate ΔT is change in temperature of (Tw-Tf) 3. Nusselt Number, Nu= hD/Kf …... (6) Where, Kf is thermal conductivity of air 4. Enhancement ratio = Nu VG / Nu flat …… (7) 5. Performance Enhancement Factor = = (Nu VG / Nu flat ) / (ΔPVG / ΔP flat )1/3 ….… (8) 2. LITERATURE REVIEW:- Ralph Kristoffer et.al. [1] - The use of flexible plates or “flags” as vortex generators inside a channel was successfully demonstrated as an alternative heat transfer enhancement technique. This paper aims to present a brief review of flag vortex generators for thermal enhancement. Although flag dynamics is widely reported, the review reveals that this heat transfer technique is not widely explored, specifically on the heat transfer performance of flags. Extensive and intensive experimental results are lacking to validate numerical and theoretical predictions. This paper further provides a non-exhaustive list of existing gaps, challenges, and potential research areas in usingflagsasvortexgeneratorsforthermal enhancement,whichaims to guide future research directions in this thermal fluid- structureproblem.Thereisa needtoconductfurtherinvestigationson this technique to fully establish its thermal characteristics. A review of existing literature revealed that the abundance of investigations concerning the dynamics of flags was notcomplementedbytheexisting reportsonthethermal characteristicsof flag vortex generators. Specifically, experimental studies on flag dynamics in confinements are not widely reported. The maximum of study are numerical in nature, essential to conduct experimental validations.The list of existinggaps,challenges and potential research areas are using flags as vortex generatorsforthermal enhancementaimstoguidefutureresearchworks in the thermal-fluid-structure problem (2017). Jae Bok Lee et.al. [2]- A two flexible flags clamped vertically insidea heatedchannel wasnumericallymodeledtoinvestigatethe dynamics of the flexible flags and their effects on heat transfer increments. The penalty immersed boundarymethodwasused to analyze the fluid–structure–thermal interaction between the surrounding fluid and the flexible flags. In the flapping mode, vortices shed from flexible flags merged and increased in values. The combined vertical structures swept out the thermal boundary layer and enhanced thermal mixing in the fluid near the heated wall and the channel core flow. Compared to rigid flags, the flexible flags significantly improve the thermal efficiency. The flexible flags with the optimal parameter set resulted in an increase up to 185% in the net heat flux and 106% in the thermal efficiency factor, compared to the baseline flow. The correlation between the vorticity and the temperature field was examined in detail using the dynamic mode decomposition (DMD) method (2017). Jae Bok Lee et.al. [3]- Two flexible flags clamped in a heated channel were numerically modeled to investigate the dynamicsof the flexible flags and their effects on heat transfer enhancement. The FAC generated a reverse karman vortex street that encouraged a greater thermal mixing as comparedtothevertical structuresgeneratedbytheflagsina symmetricconfiguration (FSC). The effects of the gap distance between the FAC (G/L) and the ratio of the channel height to the flag length (H/L) on the thermal enhancement were characterized to identify the parametersthatoptimizedthe thermal efficiency.The presenceofthe
4.
International Research Journal
of Engineering and Technology (IRJET) e-ISSN: 2395-0056 Volume: 06 Issue: 07 | July 2019 www.irjet.net p-ISSN: 2395-0072 © 2019, IRJET | Impact Factor value: 7.211 | ISO 9001:2008 Certified Journal | Page 2012 FAC with the optimal parameters increased convective heat transfer by 207% and the thermal efficiency factor by 135% compared to the baseline (open channel) flow. The thermal efficiency factor obtained in the present studywascomparedwith that obtained in the previous studies (2018). Emmanuel Virot et.al. [4]- Unsteady fluid forces are measured at the flutter and duringthepost-critical flutterofflagsplacedin a wind tunnel, focusing on the drag force and the moment around the flagpole. The evolution of these forces during flutter mode changes, induced by varying either the mass ratio or the wind velocity, is discussed by using additional high- speed imaging. For sufficiently high wind velocities, we have shown that the loss of periodicity is correlated with a strongincreasein unsteady fluid forces, leading ultimately to a tear of the flag (2013). Zheng Li et.al. [5]- Paper presents a 2D numerical study of a novel flapping vortex generator mounted on a heatsink fin for airside heat transfer enhancement. The new vortex generator is made with a thin elastic sheet bonded to the inner wall of the heatsink channel with an inclined angle. Our investigations are focused on the effects of the Young’s Modulus of the vortex generator on the oscillations of the elastic sheet, vorticity fields, and heat transferperformance.Resultsarecomparedwiththe heat transfer performances of conventional rigid Flags at two different flow velocities (Reynolds number’s). The developed flapping vortex generator can improve the average Nusselt number by 200% compared with a smooth channel with the same Reynolds number. Modal analysis is performed with transient temperature and vorticity results using dynamic modal decomposition where it is found that a steady modal behaviordirectlyinfluencesthethermal performanceofthesystem..more discrete patterns near the boundaries of the steady mode inthevorticityfieldcanenhancetheinternal convectiveheattransfer rate (2018). The present study focuses on the heat transfer enhancement using Flag as a vortex generator. Thegoal ofthepresent research is to compare, experimentally and numerically, the heat transfer characteristics and flow patterns for the smooth plate and using flags. In the present work, for both inline arrangement of flags and staggered arrangement of flags. 3. PROBLEM STATEMENT: From literature survey we can say that very less work on flag as vortex generator so it is need to investigate detailed thermal performance and need to compare with smooth plate. So, the problem statement is: “Experimental Investigation of Heat Transfer Enhancement with Inline and Staggered Flag as Vortex Generator”. 4. EXPERIMENTAL SETUP: An insulated duct with the specified dimension of 150 mm width and a height of 100 mm, length 1000mm made of glass are used for this experimental study. The smooth flat plate specimen madeupofaluminummaterial withthewidth150mm,height 150mm and having a thickness of 10 mm was placed inside the duct. The location of the specimen inside the duct were ensured such that the flowwashydro-dynamicallyfullydeveloped condition to ensure prior to the plate. Blower is used to supply cold air into duct or over the flat plate. Fig.1: Schematic of Experimental Set up.
5.
International Research Journal
of Engineering and Technology (IRJET) e-ISSN: 2395-0056 Volume: 06 Issue: 07 | July 2019 www.irjet.net p-ISSN: 2395-0072 © 2019, IRJET | Impact Factor value: 7.211 | ISO 9001:2008 Certified Journal | Page 2013 Fig.2: Experimental set up The electric heater with a capacity of 300 W had been placed beneath the aluminumplateimpartthermal energytotheairflow along with flat plate. As a result of this, the temperature was increased and as per the requirement of configuration, the heat input was controlled. There is a temperature sensor along with digital temperature indicator to measure inlet and outlet temperature of air. The temperature sensor (TS-01) was providing to measure inlet air flow temperature and temperature sensor (TS-02) was providing to measure outlet air flow temperature. The temperature sensor (TS-03 toTS06) wasproviding to measure surface temperature of plate. Anemometer is used to measure outlet velocity of air flow. Fig.3: Staggered Flag Arrangement with Test Section Inlet
6.
International Research Journal
of Engineering and Technology (IRJET) e-ISSN: 2395-0056 Volume: 06 Issue: 07 | July 2019 www.irjet.net p-ISSN: 2395-0072 © 2019, IRJET | Impact Factor value: 7.211 | ISO 9001:2008 Certified Journal | Page 2014 5. CFD RESULTS Fig4. Velocity_Profile_Without Flag Fig. 4 shows the velocity profile for smooth plate and fig.5, fig.6, fig.7 shows the velocity profiles for the flags with 0 Deg., 45 Deg. And 90 Deg. angle. Fig.8 shows the velocity profile for flag with staggered arrangement at 45 Deg. Fig 5. Velocity_Profile_With Flags at 0°
7.
International Research Journal
of Engineering and Technology (IRJET) e-ISSN: 2395-0056 Volume: 06 Issue: 07 | July 2019 www.irjet.net p-ISSN: 2395-0072 © 2019, IRJET | Impact Factor value: 7.211 | ISO 9001:2008 Certified Journal | Page 2015 Fig 6. Velocity_Profile_With Flag at 45° Fig7. Velocity_Profile_With Flag at 90° Fig 8. Velocity_Profile_With Staggered Flag at 45°
8.
International Research Journal
of Engineering and Technology (IRJET) e-ISSN: 2395-0056 Volume: 06 Issue: 07 | July 2019 www.irjet.net p-ISSN: 2395-0072 © 2019, IRJET | Impact Factor value: 7.211 | ISO 9001:2008 Certified Journal | Page 2016 Chart No. 1. Re Vs Nu for CFD Results. Pressure drops Table 2. Pressure Drop for Smooth plate and With Flag at Different angles. Chart No. 2: Reynolds’s Number Vs ΔP Maximum pressure drop occurs at Flag with 90° Re ΔP_smooth ΔP_FVG_0° ΔP_FVG_45° ΔP_FVG_90° 3750 3.24E-02 0.135325 0.0845761 0.122803 7500 1.75E-01 0.135325 0.299071 0.474965 11250 2.94E-01 0.256045 0.666726 0.970787 15000 3.13E-01 0.398072 1.13259 1.62487 18750 4.27E-01 0.555743 1.69534 2.29769
9.
International Research Journal
of Engineering and Technology (IRJET) e-ISSN: 2395-0056 Volume: 06 Issue: 07 | July 2019 www.irjet.net p-ISSN: 2395-0072 © 2019, IRJET | Impact Factor value: 7.211 | ISO 9001:2008 Certified Journal | Page 2017 W velocity Chart No. 3: W velocity for different Geometry Maximum W velocity occurs at Staggered Flag with 45°. 6. EXPERIMENTAL RESULTS: - Table 3. Experimental Re Vs Nu for Smooth Plate, Inline and Staggered Flag Geometry Chart No.4: Reynolds’s Number Vs Nusselt Number From table 3 and chart 4 the heat transfer enhancement of inline flag vortex generator is gives higher Nu varies from 16% to 28%, While the staggered flag vortex generator gives 39% to 51%moreheattransfer thanflatplate.Comparingwithstaggered and inline flags, the staggered flag gives 7% to 23% more heat transfer enhancement than inline flag as vortex generator. Re Nu_smooth Nu_inline flags Nu_stag flags 3778.378 182.2296 234.0125 271.8897 7556.757 428.41 553.8462 595.9086 11335.14 720.5077 840.1742 1023.879 15113.51 906.9328 1117.221 1372.396 18891.89 1044.214 1265.035 1556.652
10.
International Research Journal
of Engineering and Technology (IRJET) e-ISSN: 2395-0056 Volume: 06 Issue: 07 | July 2019 www.irjet.net p-ISSN: 2395-0072 © 2019, IRJET | Impact Factor value: 7.211 | ISO 9001:2008 Certified Journal | Page 2018 Chart No.5: Reynolds’s Number Vs Enhancement Ratio From chart 5. It shows that the enhancement ratio of staggered is varies from 1.3 to 1.5 while inline is varies from 1.1 to 1.4. The percentage enhancement of staggered is from 7 to 23 % than the inline arrangement. 7. CONCLUSIONS [1] This paper work shows that the Staggered Flag Arrangement with using “Flags” is leads to greater heat transfer enhancement. The main purpose of extended surface to increase the heat transfer rate. The advantages of the Flags are fluid mixing is more and boundary layer separation occurs in Channel which will help increase heat transfer Rate. [2] The Inline and Staggered Flags Arrangementgivemoreheattransfer enhancementthanthesmoothPlatebuttheStaggered Arrangement is more effective than the Inline Flags Arrangement. [3] The heat transfer enhancement of inline flag vortex generator is gives higher Nu varies from 16% to 28%, while the staggered flag vortex generator gives 39% to 51% more heat transfer than flat plate. [4] Comparing with staggered and inline flags, the staggered flaggives7%to23%moreheattransfer enhancementthaninline flag as vortex generator. 8. REFERENCES 1. Ralph Kristoffer B. Gallegos, Rajnish N. Sharma, “Flags as vortex generators for heat transfer enhancement: Gaps and challenges”, Renewable and Sustainable Energy Reviews 76 (2017) 950–962. 2. Jae Bok Lee et al, “Heat transfer enhancement by flexible flags clamped vertically in a Poiseuille channel flow”, International Journal of Heat and Mass Transfer 107 (2017) 391–402 3. Jae Bok Lee, Sung Goon Park, Hyung Jin Sung, “Heat transfer enhancement by asymmetricallyclampedflexibleflagsin a channel flow”, International Journal of Heat and Mass Transfer 116 (2018) 1003–1015 4. Emmanuel Virot, Xavier Amandolese, Pascal Hamon,“Flutteringflags: Anexperimental studyoffluidforces”,Journal of Fluid Sand Structures 43(2013)385–401 5. Zheng Li et.al, “A flapping vortex generator for heat transfer enhancement in a rectangular airside fin”, International Journal of Heat and Mass Transfer 118 (2018) 1340–1356 6. Atul Kumar Soti, Rajneesh Bhardwaj, John Sheridan, “Flow-induced deformation of a flexible thin structure as manifestation of heat transfer enhancement”, International Journal of Heat and Mass Transfer 84 (2015) 1070–1081 7. Zhen Pang, Lai-bing Jia, and Xie-zhen Yin, “Flutter instability of rectangle and trapezoid flagsinuniformflow”, Physics of Fluids 22, 121701 (2010)
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International Research Journal
of Engineering and Technology (IRJET) e-ISSN: 2395-0056 Volume: 06 Issue: 07 | July 2019 www.irjet.net p-ISSN: 2395-0072 © 2019, IRJET | Impact Factor value: 7.211 | ISO 9001:2008 Certified Journal | Page 2019 8. O. Doare, M. Sauzade, C. Eloy, “Flutter of an elastic plate in a channel flow: Confinement andfinite-size effects”,Journal of Fluids and Structures 27 (2011) 76–88 9. Sebastien Michelin, Stefan G. Llewellyn Smith, and Beverly J. Glover, “Vortex shedding model ofa flappingflag”,J.Fluid Mech. (2008), vol. 617, pp. 1–10. 10. Michael J. Shelley and Jun Zhang, “Flapping and Bending Bodies Interacting with Fluid Flows”, Rev. Fluid Mech. 2011.43:449-465.
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