Aceite Agua
cp 2200 cp 4180
T1 150 t1 22
T2 50 t2 109.719298
v 2.5 v 1.5
D 0.025
L 6
U
As 0.4712389
Q=U*As*deltaT
Delta t 33.7689938
deltaTA 40.2807018
deltaTB 28
Qgana Qb=mf_b*cp_b*(t2-t1)
Qpierde Qa=mf_a*cp_a*(T2-T1)
Qgana 550000
Qpierde 550000 Diferencia 0
U 34562.3638
,U 284 W/m^2*K Re 0.0004
As 93 m^2 Cp 4200
Frio Caliente
t1 300.15 T1 366.15
t2 311.15 T2 344.15
Q=U*As*deltaT
deltaT 49.2956213
TA 55
TB 44
Q 1169177.4 1169.1774
Mc 12.653435
Mf 25.3068701
, U, W/m^2*C 320 fm 0.04
As, m^2 6.2
Etanol Aceite
cp, J/kg 846000 cp, J/kg*C 2200
T1 78 t1 115
T2 78 t2 84.0154359
Q=U*As*DeltaT
deltaT 17.0564516
TA 37
TB 6.01543586
Q 33840
Qaceite 0.49643487 Diferencia -4.4044E-07
Qetanol 33840
NTU
cmin 2200 NTU 0.90181818
cmax
0.59416889
e 0.05694327
cp 2200 cp 4180
T1 150 t1 22
T2 50 t2 109.719298
v 2.5 v 1.5
D 0.025
L 6
U
As 0.4712389
Q=U*As*deltaT
Delta t 33.7689938
deltaTA 40.2807018
deltaTB 28
Qgana Qb=mf_b*cp_b*(t2-t1)
Qpierde Qa=mf_a*cp_a*(T2-T1)
Qgana 550000
Qpierde 550000 Diferencia 0
U 34562.3638
,U 284 W/m^2*K Re 0.0004
As 93 m^2 Cp 4200
Frio Caliente
t1 300.15 T1 366.15
t2 311.15 T2 344.15
Q=U*As*deltaT
deltaT 49.2956213
TA 55
TB 44
Q 1169177.4 1169.1774
Mc 12.653435
Mf 25.3068701
, U, W/m^2*C 320 fm 0.04
As, m^2 6.2
Etanol Aceite
cp, J/kg 846000 cp, J/kg*C 2200
T1 78 t1 115
T2 78 t2 84.0154359
Q=U*As*DeltaT
deltaT 17.0564516
TA 37
TB 6.01543586
Q 33840
Qaceite 0.49643487 Diferencia -4.4044E-07
Qetanol 33840
NTU
cmin 2200 NTU 0.90181818
cmax
0.59416889
e 0.05694327
