Dryness fraction - is anything missing here ?

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The discussion revolves around calculating the mass of steam and final dryness fraction in a closed vessel initially containing dry saturated steam at 350 kPa, which is then cooled to 200 kPa. Participants emphasize the importance of using steam tables to determine the temperature of the steam and to find the required values. Additionally, a question is posed regarding the dryness fraction at the turbine exhaust in an ideal Rankine Cycle operating at 500 kPa with a condenser pressure of 20 kPa. The calculations involve isentropic expansion and work done per kilogram of steam. The conversation highlights the necessity of understanding steam properties for accurate thermodynamic analysis.
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dryness fraction - is anything missing here ??

Hi Guys,
Got a couple of questions I need answers on.
a)A closed vessel of 0.8 m3 capacity contains dry saturated steam at 350 kPa. The vessel is cooled until the pressure is 200 kPa. Calculate
1) mass of steam in the vessel
2) final dryness fraction

b)A steam plant that operates on the ideal Rankine Cycle produces steam that is dry and saturated at 500 kPa. The condenser pressure is 20 kPa. Calculate the dryness fraction at the turbine exhaust (expansion is isentropic)
What is the work done per kilogram of steam ?

Thanks and regards
Raj
 
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rmenon said:
Hi Guys,
Got a couple of questions I need answers on.
a)A closed vessel of 0.8 m3 capacity contains dry saturated steam at 350 kPa. The vessel is cooled until the pressure is 200 kPa. Calculate
1) mass of steam in the vessel
2) final dryness fraction
Can you determine the temperature of the steam in a)? Hint: the word "saturated" is important.

AM
 
Do you mean from steam tables
 
rmenon said:
Do you mean from steam tables
Well, you could boil water at 350 kpa and see what temperature it boils at. Or you could just look it up in a steam table.

AM
 
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