Elements Of Electromagnetics
7th Edition
ISBN: 9780190698614
Author: Sadiku, Matthew N. O.
Publisher: Oxford University Press
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Question
Refrigerant R12 is used in a vapour compression cycle. The saturated vapour enters
the compressor at -18.8°C, and subsequently leaves at 75°C and 10 bar. The
saturated liquid leaving the condenser is at 10 bar. The resulting stream is throttled
and evaporated before being fed back to the compressor.
a) Determine the coefficient of performance of the refrigerator. Take the specific enthalpy,
h, at 10 bar and 36 K of superheat to be 163.7 kJ/kg
b) Obtain the isentropic efficiency of the compressor. Take the specific entropy, s, at 10
bar to be 1.188 kJ/kg
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Step 1: Introduction
VIEW Step 2: schematic circuit, T-s diagram, and p-h diagram of the vapor compression refrigeration cycle
VIEW Step 3: Evaluate properties at all state points.
VIEW Step 4: (a) Evaluate coefficient of performance of the cycle.
VIEW Step 5: (b) The isentropic efficiency of the compressor
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- An r-134a refrigerator operates a simple vapor compression cycle (SVCC). The evaporatoroperates at -10 °C, while the condenser operates at 1 MPa. R-134a flows around the system at 10 g/s.a. Graph the cycle in a P-h diagram and calculate the temperature at the exit of the compressor, assuming it is 100% isentropicallyefficient.b. Calculate the power required by the compressor (in W) and the cooling effect of the refrigerator (in kW) c. Compute for the COP of the system. What is its percent difference from the reversible efficiency?arrow_forwardQ 4) A simple vapour compression plant produces (5 tonnes) of refrigeration. The enthalpy values at inlet to compressor, at exit from the compressor, and at exit from the condenser are (183.19, 209.41 and 74.59 kJ/kg) respectively. Determine :- (i) The refrigerant flow rate, (ii) The C.O.P. (ii) The power required to drive the compressor. (iv) The rate of heat rejection to the condenser.arrow_forwardercise 6 6.1 A surface condenser is fitted with separate air and condensate outlets. A portion of the cooling surface is screened from the incoming steam and the air is passes over these screened tubes to the air extraction and becomes cooled below the condensate temperature. The condenser receives 20 000kg/hr of dry saturated steam at 36.2°C. At the condensate outlet the temperature is 34.6°C TK and at the air extraction the temperature is 29°C. The volume of air and vapour leaving the condenser is 3.8m3/min. Assume constant pressure throughout the condenser, calculate: 6.1.1 the mass of air removed per 10 000kg of steam (2.63kg); 6.1.2 the mass of steam condensed in the air cooler per minute (0.5kg/min)%3B 6.1.3 the heat rejected to the cooling water (13451kW).arrow_forward
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