00:01
In actual refrigeration cycle using r134a as the working fluid, the refrigerant flow rate is 0 .05 kg per second.
00:13
Vapor enters the compressor at 150 kilo pascal with temperature minus 10 degrees celsius.
00:22
You are given h1 is 394 .2 kilojoules per kg and entropy value is 1 .7303 .3 .3.
00:31
Kilojoules per kg kelvin and leaves at 1 .2 megapascal with 75 degrees celsius, the value for h2 454 .2 kilojoules per kg and entropy value is 1 .805 kilojoules per k .m.
00:54
The power input to the non -idiweight compressor is measured and found to be 2 .4 kilowatt.
01:04
The refrigerant enters the expansion valve at 1 .15 megapascal and 40 degrees celsius with the enthalpy 256 .4 kilojoule per kg and leaves the evaporator at 160 kilo pascal with minus degrees celsius given the value of enthalpy is 389 .8 kilojoule per kg.
01:34
Now determine the the entropy generation in the compression process, the refrigerant capacity and coefficient of performance for this cycle.
01:48
The refrigerant cycle is here.
01:53
T1 equals to minus 10 degrees celsius, p1 is 150 kioskil, t2 compressor exit is 75 degrees celsius, p2 is 1 .2 megapascal, expansion valve has p3 equals to 40 degrees celsius and p3 is 1 .15 megapascal...