We need to first determine the heat rate, using the usual formula
H = Q/t = h A ΔT
We are given h=2000 W/m²/K, but need to calculate the area A and the temp gradient ΔT. The area is
A =2*Pi*r*L
I'm assuming the 23 mm is the internal diameter, not the radius, so r=0.023/2 = 0.0115 m, with L = 10 km = 10,000 m (which sounds like a lot to me). Then
A =2*Pi*(0.0115)(10000) = 722 m².
For ΔT, the formula for a countercurrent heat exchanger is
ΔT = (ΔT1 - ΔT2)/ln (ΔT1/ΔT2), with
ΔT1 = Thot-in - Tcold-in and ΔT2 = Thot-out - Tcold-out
In this case,
ΔT1 = 95-15 = 80 °C and ΔT2= 85-70 = 15 °C
so that
ΔT =(80-15)/ln(80/15) = 38.8 °C.
Therefore,
H = 2000 (722) (38.8) = 5.6*107 W
On the food side,
H =Qfood/t = (mf/t) cf ΔT
so that
5.6*107 W = (mf/t) 3700*(70-15)
so the flow rate is
mf/t = 275 kg/s.
On the water side,
5.6*107 W = (mw/t) 4180*(95-85)
mw/t = 1340 kg/s.
Sounds like a lot of food and water to me -- are you sure this thing is 10 km long??
Nadeshiko Y.
10/31/13