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Masja [62]
3 years ago
7

At steady state, a reversible refrigeration cycle discharges energy at the rate QH to a hot reservoir at temperature TH, while r

eceiving energy at the rate QC from a cold reservoir at temperature TC. a. If TH = 13°C and TC = 2°C, determine the coefficient of performance. b. If QH = = 10.5 kW, 8.75 kW QC , and TC = 0°C, determine TH, in °C. c. If the coefficien
Engineering
2 answers:
ludmilkaskok [199]3 years ago
8 0

Answer:

a) COP_{R} = 25.014, b) T_{H} = 327.78\,K\,(54.63\,^{\textdegree}C)

Explanation:

a) The coefficient of performance of a reversible refrigeration cycle is:

COP_{R} = \frac{T_{L}}{T_{H}-T_{L}}

Temperatures must be written on absolute scales (Kelvin for SI units, Rankine for Imperial units)

COP_{R} = \frac{275.15\,K}{286.15\,K-275.15\,K}

COP_{R} = 25.014

b) The respective coefficient of performance is determined:

COP_{R} = \frac{Q_{L}}{Q_{H}-Q_{L}}

COP_{R} = \frac{8.75\,kW}{10.5\,kW-8.75\,kW}

COP_{R} = 5

But:

COP_{R} = \frac{T_{L}}{T_{H}-T_{L}}

The temperature at hot reservoir is found with some algebraic help:

COP_{R} \cdot (T_{H}-T_{L})=T_{L}

T_{H}-T_{L} = \frac{T_{L}}{COP_{R}}

T_{H} = T_{L}\cdot \left(1+\frac{1}{COP_{R}}  \right)

T_{H} = 273.15\,K \cdot \left(1+\frac{1}{5}  \right)

T_{H} = 327.78\,K\,(54.63\,^{\textdegree}C)

gregori [183]3 years ago
3 0

Answer:

a) COP = 26

b) TH = 327.6 K

c) TC = 297.3 K

Explanation:

a) TH = temperature hot reservoir = 13°C = 286 K

Tc = temperature cold reservoir = 2°C = 275 K

The coefficient of performance is

COP=\frac{1}{1-\frac{T_{C} }{T_{H} } } =\frac{1}{1-275/286} =26

b) given:

QH = 10.5 kW

QC = 8.75 kW

TC = 0°C = 273 K

\frac{Q_{H} }{Q_{C} } =\frac{T_{H} }{T_{C} } \\T_{H} =\frac{Q_{H}T_{C}  }{Q_{C} } =\frac{10.5*273}{8.75} =327.6K

c) From the COP formula we clear TC:

10=\frac{1}{1-T_{C}/300 } \\T_{C} =297.3k

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Work required = 18.45 kJ/kg

Coefficient  of performance = 3.61

Quality at the beginning of the heat  addition cycle = 0.37

Explanation:

From figure  

Q_H is heat rejection process

Q_L is heat transferred from the refrigerated space

T_H is high temperature = 50 °C + 273 = 323 K

T_L is low temperature = -20 °C + 273 = 253 K  

W_{net} is net work of the cycle (the difference between compressor's work and turbine's work)

 

Coefficient of performance of a Carnot refrigerator (COP_{ref}) is calculated as

COP_{ref} = \frac{T_L}{T_H - T_L}

COP_{ref} = \frac{253 K}{323 K - 253 K}

COP_{ref} = 3.61

From figure it can be seen that heat rejection is latent heat of vaporisation of R-12 at 50 °C. From table

Q_H = 122.5 kJ/kg

From coefficient of performance definition

COP_{ref} = \frac{Q_L}{Q_H - Q_L}

Q_H \times COP_{ref} = (COP_{ref} + 1) \times Q_L

Q_L = \frac{Q_H \times COP_{ref}}{(COP_{ref} + 1)}

Q_L = \frac{122.5 kJ/kg \times 3.61}{(3.61 + 1)}

Q_L = 95.93 kJ/kg

Energy balance gives

W_{net} = Q_H - Q_L

W_{net} = 122.5 kJ/kg - 95.93 kJ/kg

W_{net} = 26.57 kJ/kg

Vapor quality at the beginning of the heat addition cycle is calculated as (f and g refer to saturated liquid and saturated gas respectively)

x = \frac{s_1 - s_f}{s_g - s_f}

From figure

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Replacing with table values

x = \frac{1.165 kJ/(K \, kg) - 0.9305 kJ/(K \, kg)}{1.571 kJ/(K \, kg) - 0.9305 kJ/(K \, kg)}

x = 0.37

Quality can be computed by other properties, for example, specific enthalpy. Rearrenging quality equation we get

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W_{t} = |241.58 kJ/kg - 249.7 kJ/kg|

W_{t} = 8.12 kJ/kg

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W_{c} = W_{net} + W_{t}

W_{c} = 26.57 kJ/kg + 8.12 kJ/kg

W_{c} = 34.69 kJ/kg

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