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Thermal and economic investigation of straight and U-bend double tube heat exchanger with coiled wire turbulator

Treść / Zawartość
Identyfikatory
Warianty tytułu
Języki publikacji
EN
Abstrakty
EN
Experimental research has been carried out for four individual heat exchanger constructions, i.e., plain double tube, turbulized double tube, plain U-bend and U-bend with turbulator. Tests were made for the water-water system. The study covered a wide measuring range, i.e., Re = 800–9000 – on the shell side, for a constant cold water temperature of 9°C and hot water of 50°C. The heat exchangers were made from copper tubes with external diameter of 10 mm and 18 mm respectively and wall thickness of 1 mm. The helicoidal vortex generator was made from brass wire with a diameter of 2.4 mm, coil diameter of 13 mm and pitch of 11 mm. For these geometries, the values of pressure drop, heat flux and heat transfer coefficient were determined. Wire coil turbulator increased the heat transfer coefficient (HTC) over 100% and pressure drop up by 100%. The comparison of heat transfer efficiency was performed based on the number of transfer units-effectivenes (NTU-ε) method. The modified construction achieved a similar efficiency. Economic analysis of wire coil turbulator was made to validate its use in the system. It showed that a coiled wire turbulator can greatly decrease the investment cost of the double tube heat exchanger while maintaining transferred heat at a constant level.
Rocznik
Strony
17--33
Opis fizyczny
Bibliogr. 28 poz., rys., tab., wz.
Twórcy
  • Gdańsk University of Technology, Faculty of Mechanical Engineering, Narutowicza 11-12, 80-232 Gdańsk, Poland
  • Gdańsk University of Technology, Faculty of Mechanical Engineering, Narutowicza 11-12, 80-232 Gdańsk, Poland
Bibliografia
  • [1] Wang Q., Zeng M., Ma T., Du X., Yang J.: Recent development and application of several high-efficiency surface heat exchangers for energy conversion and utilization. Appl. Energy 135(2014), 748–777.
  • [2] Muszyński T., Koziel S.M.: Parametric study of fluid flow and heat transfer over louvered fins of air heat pump evaporator. Arch. Thermodyn. 37(2016), 3, 45–62.
  • [3] Andrzejczyk R., Muszyński T.: The performance of H2O, R134a, SES36, ethanol, and HFE7100 two-phase closed thermosyphons for varying operating parameters and geometry. Arch. Thermodyn. 38(2017), 3, 3–21.
  • [4] Olszewski P.: Heat recovery investigation from dryer–thermal oxidizer system in corn-ethanol plants. Appl. Therm. Eng. 81(2015), 210–222.
  • [5] Muszyński T., Andrzejczyk R., Dorao C.A.: Detailed experimental investigations on frictional pressure drop of R134a during flow boiling in 5 mm diameter channel: The influence of acceleration pressure drop component. Int. J. Refrig. 82(2017), 163–173.
  • [6] Andrzejczyk R., Muszyński T., Dorao C.A.: Experimental investigations on adiabatic frictional pressure drops of R134a during flow in 5 mm diameter channel. Exp. Therm. Fluid Sci. 83(2017), 78–87.
  • [7] Muszyński T., Andrzejczyk R., Dorao C.A.: Investigations on mixture preparation for two phase adiabatic pressure drop of R134a flowing in 5 mm diameter channel. Arch. Thermodyn. 38(2017), 3, 101–118.
  • [8] Clarke R., Finn D.P.: The influence of secondary refrigerant air chiller U-bends on fluid temperature profile and downstream heat transfer for laminar flow conditions. Int. J. Heat Mass Transf. 51(2008), 3-4, 724–735.
  • [9] Pahud D., Matthey B.: Comparison of the thermal performance of double U-pipe borehole heat exchangers measured in situ. Energy Build. 33(2001), 5, 503–507.
  • [10] Florides G., Kalogirou S.: First in situ determination of the thermal performance of a U-pipe borehole heat exchanger, in Cyprus. Appl. Therm. Eng. 28(2008), 2-3, 157–163.
  • [11] Andrzejczyk R., Muszyński T.: Performance analyses of helical coil heat exchangers. The effect of external coil surface modification on heat exchanger effectiveness. Arch. Thermodyn. 37(2016), 4, 137–159.
  • [12] Andrzejczyk R., Muszyński T.: Thermodynamic and geometrical characteristics of mixed convection heat transfer in the shell and coil tube heat exchanger with baffles. Appl. Therm. Eng. 121(2017), 115–125.
  • [13] Cengel Y.A.: Introduction to Thermodynamics and Heat Transfer. McGraw-Hill, New York 1997.
  • [14] Vitillo F., Cachon L., Reulet P., Laroche E., Millan P.: An innovative plate heat exchanger of enhanced compactness. Appl. Therm. Eng. 87(2015), 826–838.
  • [15] Cavazzuti M., Agnani E., Corticelli M.A.: Optimization of a finned concentric pipes heat exchanger for industrial recuperative burners. Appl. Therm. Eng. 84(2015), 110–117.
  • [16] Muszyński T.: Design and experimental investigations of a cylindrical microjet heat exchanger for waste heat recovery systems. Appl. Therm. Eng. 115(2017), 782–792.
  • [17] Mereu R., Colombo E., Inzoli F.: Non Linear Eddy Viscosity Model Applied to U-Bend Industrial Geometry. In: Proc. Heat Transfer, Fluid Flows, and Thermal Systems, Vol. 9, Pts. A, B, and C; ASME (2009), 215–222.
  • [18] Fratczak M., Nowak P., Czeczot J., Metzger M.: Simplified dynamical input– output modeling of plate heat exchangers – case study. Appl. Therm. Eng. 98(2016), 880–893.
  • [19] Trojanowski R., Butcher T., Worek M., Wei G.: Polymer heat exchanger design for condensing boiler applications. Appl. Therm. Eng. 103(2016), 150–158.
  • [20] Wang X., Palazoglu A., El-Farra N.H.: Proactive optimization and control of heat-exchanger super networks. IFAC-PapersOnLine 48(2015), 8, 592–597.
  • [21] Andrzejczyk R., Muszyński T.: An experimental investigation on the effect of new continuous core-baffle geometry on the mixed convection heat transfer in shell and coil heat exchanger. Appl. Therm. Eng. 136(2018), 237–251.
  • [22] Sheikholeslami M., Gorji-Bandpy M., Ganji D.D.: Review of heat transfer enhancement methods: focus on passive methods using swirl flow devices. Renew. Sustain. Energy Rev. 49(2015), 444–469.
  • [23] Liu S., Sakr M.: A comprehensive review on passive heat transfer enhancements in pipe exchangers. Renew. Sustain. Energy Rev. 19(2013), 64–81.
  • [24] Singh Yadav A.: Effect of half length twisted-tape turbulators on heat transfer and pressure drop characteristics inside a double pipe U-bend heat exchanger. Jordan J. Mech. Ind. Eng. 3(2009), 17–22.
  • [25] Baviskar P.V., Saner K.A., Salunke N.P.: To analyze the effect of varying fin shapes for microprocessor cooling. IJIRSET 5(2016), 4, 1333–1344.
  • [26] Hewitt G.F., Shires G.L., Bott T.R.: Process Heat Transfer. CRC Press, Boca Raton 1994.
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  • [28] Slavković G., Budimir S.J., Rakonjac I.M., Jarić M.S., Budimir N.J.: Techno-economic analysis of heat exchangers with parallel helical tube coils. Tech. Gaz. 21(2014), 4, 861–866.
Uwagi
PL
Opracowanie rekordu w ramach umowy 509/P-DUN/2018 ze środków MNiSW przeznaczonych na działalność upowszechniającą naukę (2019).
Typ dokumentu
Bibliografia
Identyfikator YADDA
bwmeta1.element.baztech-e8720a4a-4a63-4d41-a9f6-42ef71286411
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