mir
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hi guys... every now and then I have to go over my thermodynamics and then come back:
I have to size the length of a tube exchanger where:
1. power = 150 kw (the exchanger is dimensioned on the maintenance of temperature) = 540000000 [J/h ]2. liquid1 to be heated: m1=27 mc/h from t0° to 55°
3. liquid2 heating: m2=? mc/h from 75° to 69°
4. liquid1 and liquid2 are equal and are water (to simplify the accounts)
5. exchanger with w=100 [W/m2 K]use the classic formula: p = m cp dt and I find t0
T0 = 55°c- 540000000 [J/h ] / (27 * 1000 [kg/h] * 4186 [J/Kg K]) = 50.24 °C
calculates now the flow m2 = 540000000 [J/h ] / (4186 [J/Kg K] * (75-69) = 21500 kg/h = 21.5 mc/h
area exchanger = pot / (w * dtl)
where dtl is the logarithmic average for countercurrent flows= (69- 50.24) - (75-55) / ln (69-50.4)/(75-55)) = 19.37
area exchanger = 150000 [W] / (100 [W/m2 K] * 19.37 [K]) = 77.44 sqm
Does it seem consistent as I wrote?
thanks for the help
♪
I have to size the length of a tube exchanger where:
1. power = 150 kw (the exchanger is dimensioned on the maintenance of temperature) = 540000000 [J/h ]2. liquid1 to be heated: m1=27 mc/h from t0° to 55°
3. liquid2 heating: m2=? mc/h from 75° to 69°
4. liquid1 and liquid2 are equal and are water (to simplify the accounts)
5. exchanger with w=100 [W/m2 K]use the classic formula: p = m cp dt and I find t0
T0 = 55°c- 540000000 [J/h ] / (27 * 1000 [kg/h] * 4186 [J/Kg K]) = 50.24 °C
calculates now the flow m2 = 540000000 [J/h ] / (4186 [J/Kg K] * (75-69) = 21500 kg/h = 21.5 mc/h
area exchanger = pot / (w * dtl)
where dtl is the logarithmic average for countercurrent flows= (69- 50.24) - (75-55) / ln (69-50.4)/(75-55)) = 19.37
area exchanger = 150000 [W] / (100 [W/m2 K] * 19.37 [K]) = 77.44 sqm
Does it seem consistent as I wrote?
thanks for the help
♪