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E.T.S.I. INDUSTRIALES DE MADRID
CÁTEDRA DE TERMODINÁMICA
BOMBA DE CALOR
Madrid, mayo de 1998
Bomba de Calor
Determinación de la potencia de entrada, calor producido y eficiencia de la bomba de calor para:
-
Evaporador de agua
-
Evaporador de aire
Calcularemos previamente la constante C que dará los Julios consumidos para que se realice una revolución:
C =
=
Se selecciona un caudal del 50% en el condensador, y se toman las siguientes medidas:
| AGUA | AIRE |
t (s/rev) | 29,9 | 30,6 |
t9 (ºC) | 50,05 | 50,05 |
t7 (ºC) | 16,6 | 16 |
c (g/s)
| 10 | 10 |
Sabemos, además, que: Cp = 4,180 (J/gºC).
Con estos datos determinaremos los valores característicos de los dos tipos de evaporadores.
Evaporador de agua
=
=
=
w
=
=
=
w
=
=
=
Evaporador de aire
=
=
=
w
=
=
=
w
=
=
=
Representación de las curvas de eficiencia y calor producido para diferentes temperaturas de salida del agua del condensador (t9):
Para realizar los cálculos utilizaremos el evaporador de aire (
), e iremos reduciendo el caudal en el condensador sucesivamente.
Obtenemos las siguientes medidas:
| 100% | 75% | 50% | 25% |
t (s/rev) | 36,9 | 34,2 | 30,4 | 28,8 |
t9 (ºC) | 35 | 40 | 50 | 57 |
t7 (ºC) | 16 | 16,4 | 16,8 | 17,8 |
c (g/s)
| 20 | 15 | 10 | 5 |
100%
=
=
=
w
=
=
=
w
=
=
=
75%
=
=
=
w
=
=
=
w
=
=
=
50%
=
=
=
w
=
=
=
w
=
=
=
25%
=
=
=
w
=
=
=
w
=
=
=
A continuación representamos la gráfica
:
| t9 |
1588,40 | 35 |
1479,72 | 40 |
1387,76 | 50 |
819,28 | 57 |
Y la gráfica
:
| t9 |
2,714 | 35 |
2,343 | 40 |
1,953 | 50 |
1,092 | 57 |
Representación de un ciclo real en los diagramas p-h y t-s:
Ajustamos el caudal del condensador al 50%, y seleccionamos el evaporador de aire (
).
Tomamos los siguientes datos:
=
=
=
=
t1 = 12ºC
t2 = 66ºC
t3 = 43,5ºC
t4 = 8,5ºC
Y las presiones absolutas que se representan en los diagramas:
Pabsoluta = Pmanométrica + Patmosférica
Pabsoluta1 =
+
=
+
=
Pabsoluta2 =
+
=
+
=
1
6
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Enviado por: | El remitente no desea revelar su nombre |
Idioma: | castellano |
País: | España |