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2.The following strange equation of state has been proposed:
3. For the ESD-VDW EOS applied to square-well (γ=2) fluids at np=[0.0,0.4] z=1+4*np/(1-1.9*np)-30.4*β*Æ NIST data for Z vs. 1/T for Ar at 35 mol/L, indiccates Z=6.5-575/T Determine Ï (nm) and Æ/k (K)
1. (10 pts) Express the following in terms of Cp, Cv. P, V, T and their derivatives. Your answer may include absolute values of S if it is not associated with a derivative. (as/@P)r and (aGlOV)p 2. (10 pts) The following strange equation of state has been proposed: where a,b is a constant. Derive an expression for (OT/OP)v hintli obtain explicit function of P=f(p, T) hint 2: @TIaPW = 1 / (aPaDy 3. (30 pts) For the ESD-VDW EOS applied to square-well ( 2) fluids at η [0.0, 0.4], NIST data for Z vs. 1/T for Ar at 35 mol/L, indicates Z=65-575/T Determine Ï (nm) and ε/k (K)
2.The following strange equation of state has been proposed:
3. For the ESD-VDW EOS applied to square-well (γ=2) fluids at np=[0.0,0.4] z=1+4*np/(1-1.9*np)-30.4*β*Æ NIST data for Z vs. 1/T for Ar at 35 mol/L, indiccates Z=6.5-575/T Determine Ï (nm) and Æ/k (K)
1. (10 pts) Express the following in terms of Cp, Cv. P, V, T and their derivatives. Your answer may include absolute values of S if it is not associated with a derivative. (as/@P)r and (aGlOV)p 2. (10 pts) The following strange equation of state has been proposed: where a,b is a constant. Derive an expression for (OT/OP)v hintli obtain explicit function of P=f(p, T) hint 2: @TIaPW = 1 / (aPaDy 3. (30 pts) For the ESD-VDW EOS applied to square-well ( 2) fluids at η [0.0, 0.4], NIST data for Z vs. 1/T for Ar at 35 mol/L, indicates Z=65-575/T Determine Ï (nm) and ε/k (K)
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