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A counter-flow double-pipe heat exchanger is to heat water from 20ºC to 80ºC at a rate of 1.2 kg/s. The heating is to be accomplished by geothermal water available at 160ºC at a mass flow rate of 2 kg/s. The inner tube is thin-walled, and has a diameter of 1.5 cm. If the overall heat transfer coefficient of the heat exchanger is 640 W/(m2.ºC), determine the length of the heat exchanger required to achieve the desired heating using the effectiveness-NTU method. Take the specific heat of geothermal water to be 4.31 kJ/(kg.ºC) and that of water to be 4.18 kJ/(kg.ºC).
Here the cold fluid (denoted as subscript c) is water and hot fluid (denoted as subscript h) is geothermal water.
Given: Initial and final temperature of water respectively, t1= 200C and t2= 800C
Mass flow rate of water, c=1.2 kg/s
Initial temperature of geothermal water, T1=1600C
Mass flow rate of geothermal water, h=2 kg/s
Overall heat transfer coefficient, U= 640 W/m20C
Diameter of the tube, D=1.5 cm= 0.015 m
Specific heat of geothermal water, Cph=4.31 kJ/kg0C
Specific heat of water, Cpc=4.18 kJ/kg0C
Step 1: Determine the heat capacity flow rate of hot and cold fluid to get the minimum value of specific heat flow rate.
Heat capacity flow rate of hot fluid, Ch is Ch= hCph
Ch= 2 kg/s*4.31 kJ/kg0C=8.62 kJ/s0C
Ch= 8.62 kW/0C
Heat capacity flow rate of cold fluid, Cc is Cc= cCpc
Cc = 1.2 kg/s*4.18 kJ/kg0C= 5.016 kJ/s0C
Cc = 5.016 kW/0C
As Cc < Ch, the minimum and maximum value will be Cmin= 5.016 kW/0C and Cmax = 8.62 kW/0C respectively.
The capacity ratio, c=Cmin/Cmax= 5.016/8.62=0.5819=0.582
c = 0.582
Step 2: Calculate the maximum heat transfer rate and actual heat transfer rate.
Maximum heat transfer rate, is calculated using the expression
The actual heat transfer rate, is calculated using the expression
Step 3: Calculate Effectiveness of heat exchanger and NTU
The effectiveness of a heat exchanger is
For a counter flow double pipe heat exchanger, Number of Transfer Units, NTU is obtained from the effectiveness relation for heat exchanger
where c is the Capacity Ratio (Determined in earlier steps)
Step 4: Length of heat exchanger required to achieve the desired heating is
where L is the Length of the heat exchanger
D is the Diameter of the tube
As is the Heat Transfer Surface Area
As is obtained from the expression
Thus the length of the heat exchanger for the calculated heat transfer surface area is
Therefore, the length of heat exchanger required is L= 108.45 m which can be approximated to 109 m.