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A design for purifying helium consists of an adiabatic process that splits a helium stream containing...

A design for purifying helium consists of an adiabatic process that splits a helium stream
containing 30-mole-percent methane into two product streams, one containing 97-mole-percent helium
and the other 90-mole-percent methane. The feed enters at 10 bar and 117°C; the methane-rich product
leaves at I bar and 27°C; the heHum-rich product leaves at 50°C and 15 bar. Moreover, wort is
produced by the process. Assuming heHum an ideal gas with Cp = (S/2)R and methane an ideal gas
with Cp = (9/2)R., ealculate the total entropy change of the process on the basis of I mol of feed to
confirm that the process does not violate the second law.

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Step:-1 Griven 971. Helium 34. Methane stream 1 Souc (Ti) is bar (P.) Imple feed 30-4. Methane 70% Helium to bar (PP) 117°c (For an Ideal Gas, Enkopy change of System to as) System & lm Tz - R lm Pz Т) en P at constant pressure G = Heat Capacity T2,Entropy change of Helium in steam 1 (AS R lm Pa He G lm Ta He Pf 5 504273 R lm R lm is 2 10 117 +273 He - 3.9 Ilmol. K 3.37(AS) - 10.42 Ilmol. K Entropy change of Helium in stream 2 He 45) lim Ti = Rlm Pe > CHE TF Anlasts 56 R lm 37+973 R lm 1 2 102 117 + 2+ 3 –9.81 Il meil - K 2 + 19. 14 Il mol. K САҚ leader 9.33 Ilmol. K Basis 1 mole feed (AS) CHA 9% R lm 27+273 - R. ltotal Entropy change of Helium, Mhle [cas), 0.7 miles (-7.27 + 13.69] 5/male-k (AS) He 2 He + (As) *e] 2 (AS) 2 He 4.49 Ilk tEnkopy change of surroumdings, (AS) Sures ♡ Ts Q = Heat transfer Ts - Surrounding / Resewiol temperatūreSince Adiabatic process, Q-0 (AS) z 0 surroundings total Entropy of Universe (AS) System + AS) Surrol 2 4.163 JIK + 0 JK (As)

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