02193nam a2200265 a 4500 vtls000052287 KUKTEM 20251114204445.0 110325t2010 my da f m 000 0 eng d THE0006427(Local) 201905131519 amirul 201211011408 Fida 201107140041 VLOAD 201103250947 ida 201103250945 ida UMP TJ853 .B57 2010 rs Bc. Muhammad Bisharul Hafi Ab Jalil Determination of heat transfer coefficient using experimental values of pressure drop of a single phase fluid / Muhammad Bisharul Hafi Ab Jalil Kuantan, Pahang : UMP, 2010 xv, 71 p. : ill. (some col.) ; 30 cm. + 1 CD-ROM Project paper (Bachelor of Mechanical Engineering) -- Universiti Malaysia Pahang - 2010 Bibliography: p. 50-53 Analogical procedure to obtain the heat transfer coefficient for fluid flowing inside tube in turbulent range with carbon nanotubes is carried out. A regression equation valid for both water and nanofluid is developed by making use of Colburn analogy to estimate the Nusselt number. Heat transfer coefficient and pressure drop with carbon nanotubes has been analogically determined with different Prandtl number and volume concentration. Based on the analysis, the regression equation showed considerable deviation with the Gnielinski correlation and considered reliable in turbulent flow for single-phase fluid. The results also showed that convective heat transfer flow in plain tube is enhanced significantly by the existence of carbon nanotubes when compared with water using the regression equation developed. It is also observed that heat transfer coefficient for carbon nanotubes having volume concentration of 0.1% is 48.16% higher compared with water at 20,000 Reynolds number. Heat transfer coefficient is also enhanced with the increase of Prandtl number and volume concentration with maximum value of 0.5%. Nanofluids Fluidic devices Heat Transmission 0 0 0 1 20000 20000 2019-09-04 0 TJ853 .B57 2010 rs Bc. 0000053873 2019-09-04 00:00:00 1 2019-09-04 PSM 0 0 0 1 20000 20000 2019-09-04 0 CD 4952 | TJ853 .B57 2010 rs Bc. 0000053874 2019-09-04 00:00:00 1 2019-09-04 PSM VIRTUA40 2377 2383 VTLSSORT0080*0200*0400*0900*1000*2450*2600*3000*5020*5040*5200*6500*6501*6502*9992