-1 Oil with speed 7260 kg / h and heat capacity c (oil) = 2.07 kJ kgrK cooled from 394.3 K to 338.9 K in a countercurrent heat exchanger where water enters with temperature 294.3 K and out with temperature 306.4 K. Calculate the flow rate (is equal to the mass flow) of the water and the heat transfer coefficient, U, when the area of the heat exchanger is 5.22 m. The heat capacity of water is = 4,183 kJ kg K -1 -1
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- Hot water flowing at 0.015 m3/min enters the tube side of a counter current shell & tube heat exchanger at 80 C and leaves at 50 C. Cold oil flowing thru the shell at 0.05 m3/min, with density 800 kg/m3 and specific heat of 2.0 kJ/kg K, enters at 20 C. Consider water specific heat at 4.2 kJ/kg K and density of 988 kg/m3 at above condition, what is the approximate Log Mean Temperature Difference (LMTD)? Show the temperature profile completely labeled.In a countercurrent double-pipe heat exchanger, the hot oil entering the inner tube at 420 K with a flow rate of 60 g/s is required to be cooled to 320 K. In the space between the outer tube and the inner tube of the heat exchanger, cooling water flows at the same linear speed as the oil. Cooling water enters the heat exchanger at 290 K. The inner tube inner diameter of the heat exchanger is 25 mm and the outer tube inner diameter is 40 mm. Calculate the length of the heat exchanger. The oil side heat transfer coefficient is 1.6 kW/m2 K, and the water side heat transfer coefficient is 3.6 kW/m2 K. The densities of oil and water can be taken as 0.8 and 1.0 g/cm3, respectively, and the specific heats of oil and water can be taken as 2.0 and 4.2 kJ/kg K, respectively. Wall effects can be neglected. Flow cross-sectional area = (PI)*D2 /4 F2Hot water at 60℃ is cooled to 36℃ through the tube side of a 1–shell pass and 2-tube passesheat exchanger. The coolant is also a water stream, for which the inlet and outlet temperaturesare 7℃ and 31℃, respectively. The overall heat transfer coefficient and the heat transfer areaare 950 W/m2 K and 15 m2 , respectively. Calculate the mass flow rates of hot and cold waterstreams in steady operation. (Answers: 3.63 kg/s for both stream)
- In order to cool a mass flow rate of 25 Kg/h of air (cp = 1060 J/Kg oC) at 300 oC, it is passed through the tube side of a counter flow heat exchanger with a length of 2 m and 2.54 cm tube outer diameter. The cooling water, (cp = 4182 J/Kg oC and r = 1000 Kg/m3), enters the heat exchanger at a temperature of 30 oC with a volume flow rate of 0.3 Litre/min. If the overall heat transfer coefficient, U, is 5.83 W/m2 oC and the effectiveness of the heat exchanger 60 %, calculate the following: The heat transfer rate, The exit temperatures of both the water and the air, The surface area of the heat exchanger, The number of tubes used in the heat exchanger The capacity rate ratio.Explain how the maximum possible heat transfer rate ???? in a heat exchanger can be determined when the mass flow rates, specific heats, and the inlet temperatures of the two fluids are specified. Does the value of Q.max depend on the type of the heat exchanger?Hot fluid enters at a flow rate of 3 kg/sec with an inlet temperature of 150 C while cold fluid enters 5 kg/sec and with an inlet temperature of 60 C. Determine the maximum heat transfer that can happen during the heat exchange process? Take specific heat value of the fluid as 2000 J/(kgC) not sufficient information 150 kW 1 MW 540 kW none of the given 900 kW
- Water stream (density 997 kg/m3) is fed to the shell side of a shell and tube heat exchanger in a mass flow rate of 561.9 t/h. The inner diameterof the shell is 45 cm, it contains 70 tubes of diameter 25/30 mm.Give the linear velocity at the shell side in m/s.The hot akapkan, which enters the inner pipe of a double-pipe exchanger at a speed of 5200 kg/h at 120 °C, is desired to be cooled to 22 "C. In order to cool the hot fluid, the hot fluid is fed tap water at 15 °Dec with a speed of 10780 kg/h between the inner and tooth pipes in the opposite direction. Calculate the length of the double-pipe heat exchanger to be used as a heat exchanger in these conditions.(L?) data: D0=13.8cm Di=12cm K pipe=12w/m.k hi=22w/m^2 k. ho=36w/m^2k CP,hot=2.2 kj/kg.k , CP ,water =1.3 KJ/Kg.kAir enters a cooler at 1450C and at a pressure of 3 bar and is cooled to 450C by passing through tubes of 10 mm inside diameter surrounded by water which enters the cooler at 150C and exits at 300C. Assuming the heat exchanger is counter flow, find: I) The mean temperature difference. ii) If the air velocity is limited to 6.5 m/s, what is the required length of tube? Neglect the resistance of the tube and assume water side heat transfer coefficient is 232 W/m2K.
- A shell and tube heat exchanger is designed as a counter to cool a mass flow rate of 60 kg/h of engine oil (cp = 1060 J/kg oC) from 300oC to 150oC. The cooling water, cp = 4182 J/kgoC, enters the tube side (Length is 1.75 m and Outer diameter is 2.54 cm) at a temperature of 20oC. If the overall heat transfer coefficient, U, is 10.83 W/m2o C and the Capacity Ratio of the Heat Exchanger is 2.4, calculate the following: a)The heat transfer rate,b)The mass flow rate of the cooling water in the units of (kg/h),C)The surface area of the heat exchanger,In order to cool a mass flow rate of 55 Kg/h of air (cp = 1060 J/KgoC) at 300o C, it is passed through the tube side of a counter flow heat exchanger with a length of 2 m and 2.54 cm tube outer diameter. Thecooling water, (cp = 4182 J/Kg o C and ρ = 1000 Kg/m3 ), enters the heat exchanger at a temperature of 30o C with a volume flow rate of 0.6 Litre/min. If the overall heat transfer coefficient, U, is 5.83 W/m2oC andthe effectiveness of the heat exchanger 60 %, calculate the following:a. The heat transfer rate,b. The exit temperatures of both the water and the air,c- The surface area of the heat exchanger,A long thin-walled double-pipe heat exchanger with tube and shell diameters of 2 cm and 4 cm, respectively, is used to condense refrigerant-134a by water at 20 C. The refrigerant flows through the tube, with a convection heat transfer coefficient of hi = 4000 W/m2 K.A 1-mm-thick layer of limestone (k = 1.2 W/mK) forms on the outer surface of the inner tube. Water flows through the shell at a rate of 0.4 kg/s. Determine the overall heat transfer coefficient U of this heat exchanger with and without the fouling factor, and the error in U introduced by neglecting the fouling factor. Comment the fouling effect on this heat exchanger.