Ammonia gas is compressed from 21°C and 200 kPa to 1,000 kPa in an adiabatic compressor with an efficiency of 0.79. Estimate the final temperature, the work required, and the entropy change of the ammonia. The heat capacity coefficients are given in the table below. Heat Capacities of Gases in the Ideal-Gas State* Constants in equation C²¾³/R = A + BT+CT² + DT-² for T (K) from 298 K to Tmax Chemical species Ammonia P298 Tmax C/R A 103 B 106 C 10-5 D NH3 1800 4.269 3.578 3.020 -0.186 The final temperature is K. The work required is kW. The entropy change is J.mol-1.K-1

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Ammonia gas is compressed from 21°C and 200 kPa to 1,000 kPa in an adiabatic compressor with an efficiency of 0.79. Estimate the
final temperature, the work required, and the entropy change of the ammonia. The heat capacity coefficients are given in the table
below.
Heat Capacities of Gases in the Ideal-Gas State*
Constants in equation C²¾³/R = A + BT+CT² + DT-² for T (K) from 298 K to Tmax
Chemical species
Ammonia
P298
Tmax C/R A
103 B
106 C
10-5 D
NH3
1800
4.269
3.578
3.020
-0.186
The final temperature is
K.
The work required is
kW.
The entropy change is
J.mol-1.K-1
Transcribed Image Text:Ammonia gas is compressed from 21°C and 200 kPa to 1,000 kPa in an adiabatic compressor with an efficiency of 0.79. Estimate the final temperature, the work required, and the entropy change of the ammonia. The heat capacity coefficients are given in the table below. Heat Capacities of Gases in the Ideal-Gas State* Constants in equation C²¾³/R = A + BT+CT² + DT-² for T (K) from 298 K to Tmax Chemical species Ammonia P298 Tmax C/R A 103 B 106 C 10-5 D NH3 1800 4.269 3.578 3.020 -0.186 The final temperature is K. The work required is kW. The entropy change is J.mol-1.K-1
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