To determine the overall heat transfer co –efficient in Counter flow heat exchanger
Length of the heat exchanger= 1800 mm
Inner Copper Tube (ID) = 12 mm
Inner Copper tube (OD) = 15 mm
Outer GI tube Id = 40 mm
Heat content of Hot Water
Qh = mh Cph (Thi- Tho) watts
Where,
mh - Mass flow rate of hot water, kg,/sec
Thi - Temperature of hot water inlet (°C)
Tho - Temperature of hot water outlet (°C)
Cph - Specific heat of hot water in kJ/kg K
Heat content of cold water:
Qc = mc Cpc (Tco - Tci) watts
Where,
mc - Mass flow rate of cold water, kg,/sec
Tci - Temperature of inlet cold water (°C)
Tco - Temperature of outlet cold water (°C)
Cpc - Specific heat of cold water in kJ /Kg K
Q = Q h + Q c/2 KJ/Sec
Logarithmic Mean Temperature Difference ( LMTD):
LMTD (ΔTm) = (δT i-δT o)
In (δT i-δT o)
= (Tho-Tco) - (Thi-Tci)
In (Tho-Tco/Thi-Tci)
Where,
δT i = T ho-T co
δT o = T hi-T ci
Overall Heat Transfer Co-Efficient
Ui - = Q/A iΔTmW/m2°C
Where,
Ui - Overall heat transfer coefficient based on inner surface area in W/m2°
Ai -Inner surface area in m2
ΔTm - Logarithmic mean temperature difference
Uo - = Q/A oΔTmW/m2°C
Where,
Uo - Overall heat transfer coefficient based on inner surface area in W/m2°C
Ao -Outer surface area in m2
ΔTm - Logarithmic mean temperature difference
Effectiveness of Heat Exchanger = mc Cpo(T o = T co-T ci)
mh Cph(T hi - T ho)
The effectiveness of heat exchanger for Counter flow is ______ _ __
The overall heat transfer co –efficient based on inner surface area of heat exchanger is ___
The overall heat transfer co –efficient based on outer surface area of heat exchanger is ___
Heat exchanger is equipment which transfers the energy from a hot fluid to cold fluids, with maximum rate & minimum investment
LMTD is defined as the temperature difference which, if constant, would give the same rate of heat transfer as actually occurs under variable conditions of temperature difference.
For evaporators & condensers, LMTD for parallel & counter flow is equal/same.
If heat capacity of both fluids is same, then LMTD is equal to temperature difference at either ends.
Relative direction of motion of fluids: Parallel, Counter & Cross flow.
NTU method is necessary if outlet temperature of both fluids is not known as priority.
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