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IRJET- Experimental Investigation of Pipe in Pipe Tube Heat Exchanger using Sio2 Nanofluid
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IRJET- Experimental Investigation of Pipe in Pipe Tube Heat Exchanger using Sio2 Nanofluid
1.
International Research Journal
of Engineering and Technology (IRJET) e-ISSN: 2395-0056 Volume: 05 Issue: 08 | Aug 2018 www.irjet.net p-ISSN: 2395-0072 © 2018, IRJET | Impact Factor value: 7.211 | ISO 9001:2008 Certified Journal | Page 1436 Experimental Investigation of Pipe in Pipe Tube Heat Exchanger Using Sio2 Nanofluid Akash A.Dhobale1, Dr.J.A.Hole2 1ME student, Department of Mechanical Engineering, JSPM’s NTC narhe, Maharashtra, India. 2Professor, Department of Mechanical Engineering, JSPM’s Tathawade , Maharashtra, India. -----------------------------------------------------------------------***-------------------------------------------------------------------- Abstract - Pipe in pipe tube heat exchanger system was design and constructed to investigate the behavior of the nanofluid SiO2 with respect to the base fluid. Heat transfer characteristicswere measured. Experimental setupconsists of outer M.S pipe, inner aluminum pipe, SiO2 nanofluid with 2% vol concentreat ,100nm size and water is a base fluid. Based on results heat transfer characteristics of the nanofluid improve the performance of the heat exchanger. By adding the nanopartical in the base fluid which increases the heat transfer characteristics and results in larger the heat transfer coefficient as compare to base fluid. In this paper we see the how nanofluid affects in the heat transfer. Key Words: heat transfer characteristics, Nanofluid, pipe in pipe tube heat exchanger, Effectiveness . 1. INTRODUCTION Pipe in pipe tube heat exchanger is a mechanicaldevice,used to transfer of heat between two fluids at different temperatures. This types of heat exchanger widely used in industries. Now a day for heat transfer enhancement, nanofluid is used. The first time nanofluid was defined in 1995, when Choi, working in a research project at Argonne National Laboratory. Nanofluid is the mixture of nanopartical and base fluid. Nanopartical have the highly thermal conductivity, so it increasesthe thermal propertyof the base fluid (water or glycol). This exchanger used in food industries, petroleum industries, oil industries, thermal power plant and chemical industriesetc. For increasingheat exchanger performance now a day’s nanofluidiswidelyused in heat transfer devices. Now companies trying to find high heat transfer in compact heat exchanger. So by using nanofluid with variousconcentrationswillincreasestheheat transfer rate at compact heat exchanger. So nanofluid is helpful for designing the heat exchanger which transfers more heat in compact size as compare to conventional heat heat exchanger. In this pipe in pipe tube heatexchangerSiO2 nanofluid with 100nm size at 2% vol. concentration is used. 1.1 Materials Selection By studying the research, the many different nanofluid is used in heat exchanger like CuO, Al2O3 , ZnO etc. Base fluid mostly used for preparation of the nanofluid are water , ethylene glycol , engine oil etc. from the above studywehave select the pipe in pipe tube heat exchanger with SiO2 nanofluid. Table -1: Thermal properties of water and SiO2 nanofluid Table -2: Material Specification 2. EXPERIMENTAL SETUP Fig -1: Line diagram of the setup The pipe in pipe tube heat Exchanger consists of two pipes. Outer pipe made up of M.S having outer diameter 76.2mm and inner diameter 74.2 mm and 1m long. Inner pipe made up of aluminum having inner diameter 23.4mm and outer diameter 25.4mm and 1050mm long. On the inletofonepipe valve is provided to open and close alternatively for parallel and counter flow operation. Two tanks are used for store cold and hot fluid. Two pumps is used for pumping the fluid Sr. No. Property water SiO2 1 density(Kg/m3) 998 2220 2 Specific Heat (J/kg-k) 4187 745 3 Thermal conductivity (W/m.K) 0.58 1.4 4 Viscosity (Pa.s) 0.0019 -
2.
International Research Journal
of Engineering and Technology (IRJET) e-ISSN: 2395-0056 Volume: 05 Issue: 08 | Aug 2018 www.irjet.net p-ISSN: 2395-0072 © 2018, IRJET | Impact Factor value: 7.211 | ISO 9001:2008 Certified Journal | Page 1437 in the heat exchanger it pump maximum 10.lpm of fluid. 2500 W one immersion heater is used, to heat the fluid. For flow measuring one rota meter is used to measure the cold fluid flow. Four K type thermocouple is used for measuring temperature of the inlet and outlet of the both fluids. For temperature indicating digital temperatureindicatorisused. Fig -1: Experimental setup 2.1 Analysis of pipe in pipe tube Heat Exchanger The analysis of the heat exchanger as following [7]: i) Hot fluid heat transfer rate Qh = mh×Cph×(Thi – Tho ) ii) Cold fluid heat transfer rate Qc = mc×Cpc×(TCo – TCi ) Where (Thi, Tho) is the inlet and outlet temperature of the hot fluid. And (TCi, TCo ) is the inlet and outlet temperatureof the cold fluid. mhand mC is the mass flow rate of hot andcold fluid. Qavg = iii) Effectiveness of the Heat Exchanger Ɛ = iv) Density of nanofluid calculated 𝜌nf = (1- φ) ×𝜌bf + φ𝜌p v) Specific heat of the nanofluid Where 𝜌nf, Cpnf is the density and specific heat of the nanofluid respectively. Φ is the weight concentration of the of the nanopartical in volume of the base fluid.Cpnp and Cpbf is the specific heat of the nanopartical and base fluid respectively. 3. RESULTS AND DISCUSSION In order to study of pipe in pipe tube heat exchanger, the nanopartical increase the thermo physical properties of the base fluid. By using nanofluid we will increase the heat transfer characteristicsof the exchanger. Nanofluidgivesthe good result than water. Also the increases or decreases of the mass flow rate, is affect on heat transfer rate. Table -3: Observation table Results are shown in graphical forms, as they following: Chart -1: Time vs. temperature difference It is the combine graph of water vs. SiO2 nanofluid. This graph clearly shows that the difference between nanofluid and water. In this we see that time increases at specific interval there is increasesthe temperature difference.Sowe see that as compare to water nanofluid gives more temperature difference.
3.
International Research Journal
of Engineering and Technology (IRJET) e-ISSN: 2395-0056 Volume: 05 Issue: 08 | Aug 2018 www.irjet.net p-ISSN: 2395-0072 © 2018, IRJET | Impact Factor value: 7.211 | ISO 9001:2008 Certified Journal | Page 1438 Chart -2: Mass flow rate vs. temperature difference Chart 2. Shows that comparison between mass flow rate vs. temperature difference of the water and nanofluid. Nanofluids have more thermal conductivitythanwater.That means it will conduct more heat than water. In the graph we see that if we decrease the mass flow rate of the nanofluidor cold water there is increases the temperature difference of the heat exchanger. Means that if we vary the flow of the fluid there is affect on the outlet temperature of the heat exchanger. Chart -3: Mass flow rate vs. Effectiveness The chart shows that the effectiveness of the water and nanofluid. And we see the combine result of the mass flow rate vs. effectiveness of the heat exchanger of water and nanofluid. Effectiveness of the heat exchanger is dependson temperature difference of the hot water and temperature difference of the inlet hot and inlet nanofluid fluid. So as we discus above if we vary the mass flow rate there is also vary the temperature difference of the hot water and nanofluid. Means that if we vary or reduce the mass flow rate of the working fluid, there is vary or increase the effectiveness of the heat exchanger. Effectiveness of the heat exchanger should be lies in between 0 to 1 Chart -4: Time vs. average heat transfer rate The chart 4 shows that water and nanofluid combine result of time vs. average heat transfer rate. Heat transfer rate of the heat exchanger isdepends on the temperaturedifference of the fluid. So chart 4 shows that if we increases the time at a specific interval there is increases theaverageheattransfer tare of the heat exchanger. Chart -5: Mass flow rate vs average heat transfer rate It is seen that effect of mass flow rate on average heat transfer rate of the heat exchanger. From chart 5 we see as we decrease the mass flow rate, there is average heat transfer rate of the nanofluid increases. 3. CONCLUSIONS Heat transfer rate is directly proportional to Reynolds number. Pressure drop increases with increase in volume concentration. Spherical shaped nano-material give better heat transfer rate than other shapes. From the Experimental investigation we observed that thermal conductivity of the nanofluid is greater than water. Inlet Temperature of the hot and cold fluid willalsoaffecton the heat transfer rate. Also by varying the mass flow rate we can control the heat transfer rate and effectiveness of the heat exchanger. Increasing the time is also increasestheheat transfer rate. By using SiO2 nanofluid asa cooling fluid inthe pipe in pipe tube heat exchanger Effectiveness of the heat exchanger increased by 23.10% as compare to the water.
4.
International Research Journal
of Engineering and Technology (IRJET) e-ISSN: 2395-0056 Volume: 05 Issue: 08 | Aug 2018 www.irjet.net p-ISSN: 2395-0072 © 2018, IRJET | Impact Factor value: 7.211 | ISO 9001:2008 Certified Journal | Page 1439 REFERENCES [1] Tareq Salameh, Muhammad Tawalbeh ,MamdouhElHaj Assad, Experimental and Numerica Study on Heat Transfer Enhancements of Concentric Tube Heat Exchanger Using Water Based Nanofluids, 5th International Conference on Renewable Energy: Generation and Applications (ICREGA) , 2018 [2] A.A. Rabienataj Darzi , Mousa Farhadi , Kurosh Sedighi , Rouzbeh Shafaghat , Kaveh Zabihi Experimental investigation of turbulent heat transfer and flow characteristicsofvSiO2/water nanofluidwithinhelically corrugated tubes , International Communications in Heat and Mass Transfer 39 (2012) 1425–1434 [3] S.Gh. Etemad , B. Farajollahi , Heat Transfer Of Nanofluilds In A Shell And Tube Heat Exchanger, International Journal of Heat and Mass Transfer · January 2010,https://www.researchgate.net/publication/23236 5233 [4] Harika Kallalu, Likhitha Tummala , Fabrication of Shell and Tube Heat Exchanger using Helical Bafflesbasedon Kern's Principle , International Journal of Current Engineering and Technology, July 2017, E-ISSN 2277 – 4106,P-ISSN2347– 5161,https://www.researchgate.net/publication/31609 7330 [5] Dr.Hiregoudar Yerrennagoudaru1, Manjunatha.k 2, B.Vishnu Prasad 3 , Sandeep .k 4, Nano Fluids for Heat Exchanger , International Journal of EngineeringScience and Innovative Technology (IJESIT) Volume 5, Issue 4, July 2016 [6] A.GopiChand1, A. V. N. L. Sharma2, G. Vijay Kumar3, A.Srividya4 , Thermal Analysis Of Shell And Tube Heat Exchanger Using Mat Lab And Floefd Software , International Journal of Research in Engineering and Technology (IJRET) , Volume: 01 Issue: 03 | Nov-2012, http://www.ijret.org [7] Bharat B. Bhosle1, Prof.D.N.Hatkar2, Analysis of Heat Transfer Enhancement of Heat Exchanger using Nanofluid. International Research Journal of Engineering and Technology (IRJET) , Volume: 04 Issue: 04 | Apr -2017 [8] Adnan M. Hussein1,4, R.A. Bakar1,2, K. Kadirgama1,2 and K.V. Sharma3 , Experimental Measurement Of Nanofluids Thermal Properties. InternationalJournalof Automotive and Mechanical Engineering (IJAME) ISSN: 2229-8649 (Print); ISSN:2180-1606(Online);Volume7, pp. 850-863, January-June 2013 [9] Suleiman Akilua, Aklilu Tesfamichael Bahetaa, Mior Azman M.Saida, Alina Adriana Mineab,K.V. Sharmac , Propertiesof glycerol and ethylene glycolmixturebased SiO2-CuO/C hybrid nanofluid for enhanced solarenergy transport. (Elsvier) Solar Energy Materials and Solar Cells 179 (2018) 118–128 [10] N. K. Chavda, Effect of Nanofluid on Heat Transfer Characteristics of Double Pipe Heat Exchanger: Part-Ii: Effect Of Copper Oxide Nanofluid. IJRET: International Journal of Research in Engineering and Technology eISSN: 2319-1163 | pISSN: 2321-7308, Volume: 04 Issue: 04 | Apr-2015
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