Temperature (K) 100 77 (liq.) 77 (gas) 200 300 400 500 600 1 bar -3407 2161 2856 5800 8717 11,635 14,573 17,554 100 bar -1946 4442 8174 11,392 14,492 17,575 Table 4.5. Molar enthalpy of nitrogen (in joules) at 1 bar and 100 bars. Excerpted from Lide (1994).

Elements Of Electromagnetics
7th Edition
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Author:Sadiku, Matthew N. O.
Publisher:Sadiku, Matthew N. O.
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Consider an ideal Hampson-Linde cycle in which no heat is lost to the environment.

Use the data in attached Table to calculate the fraction of nitrogen liquefied on each pass through a Hampson-Linde cycle operating between 1 bar and 100 bars, with an input temperature of 300 K. Assume that the heat exchanger works perfectly, so the temperature of the low pressure gas coming out of it is the same as the temperature of the high-pressure gas going in. Repeat the calculation for an input temperature of 200 K.

Temperature (K)
100
77 (liq.) 77 (gas)
200
300
400
500
600
1 bar
-3407
2161
2856
5800
8717
11,635
14,573
17,554
100 bar
-1946
4442
8174
11,392
14,492
17,575
Table 4.5. Molar enthalpy of nitrogen (in joules) at 1 bar and 100 bars.
Excerpted from Lide (1994).
Transcribed Image Text:Temperature (K) 100 77 (liq.) 77 (gas) 200 300 400 500 600 1 bar -3407 2161 2856 5800 8717 11,635 14,573 17,554 100 bar -1946 4442 8174 11,392 14,492 17,575 Table 4.5. Molar enthalpy of nitrogen (in joules) at 1 bar and 100 bars. Excerpted from Lide (1994).
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