EXPERIMENTS TO MEASURE (u O – u)
I. EXPERIMENTS TO MEASURE (u O – u)
It is possible to measure the difference (u o – u) for real gases using the Washburn ex- periments (see Chapter 2). A mass m of high pressure gas stored in a tank A is discharged through s narrow tube C into the atmosphere at B ( Figure 12 ). The tank and the tube are main- tained in a constant temperature bath D. Recall the following relation from Chapter 2, during a short period of time “dt”.
(a) Since the discharged gas pressure is atmospheric,
m du + u dm = δQ – dm(h(T B ,P o ) + ke o ).
h(T B ,P o )=h o (T B ).
Ignoring the kinetic energy ke, Eq.(a) becomes d(mu) = δQ+ dm h o (T B ), i.e., m 2 u 2 –m 1 u 1 = Q + (m 2 –m 1 )h o (T B ). Where states (1) and (2) are initial and final states of tank A With u 2 =u 0 , m 2 =m 0 ,
(m 0 u 0 (T B )–m 1 u 1 (T 1 ,P 1 )) = Q + (m 0 –m 1 ) RT B and m 0 = v/v 0 , with m 1 = v/v 1
V/v o u o – V/v 1 u 1 = Q + (V/v o – V/v 1 )(u o + RT B ), i.e.,
u res
Figure 12. Washburn experiments (from A. Kestin, A Course in Thermodynamics, McGraw Hill, NY, 1979, p 262, Volume I. With permission.).
u o (T B )–u 1 (T B , P) = Q v 1 /V + (RT B v 1 /v o – RT B )=Qm 1 + (P o V/m 1 – RT B ). (b) With known Q, V, T B and P O we can determine the difference between the ideal and real gas
internal energies in this manner. The “P” in tank A can be altered and corresponding u 0 – u 1 can be determined from Eq. (b). Likewise, using the expression h = u + Pv,
h o (T B )–h 1 (T B , P) = Q m 1 – (P – P o ) V/m 1 .
The Washburn coefficient ( ∂u/∂P) T represents the slope of the difference (u o (T B ) – u 1 (T B , P)) with respect to pressure. The slopes for molecular oxygen and air, respectively, tend
to approach values of 6.51 and 6.08 kJ kmole –1 bar –1 as P →P o . Differentiating Eq. (60), we obtain the relation
∂P = –(3/2)(a/(bT 2 ∂v/∂P)/(v (1+b/v)). (c) Since v has a relatively large value (as P →P o ), neglecting higher order terms in v,
(T) – u(T,v))/ ∂(u 1/2
∂(u 2 o (T) – u(T,v))/ ∂P = –(3/2)(a/(bT ))( ∂v/∂P) T,v →∞ /v . Using the expression for ∂v/∂P given in Chapter 6 for RK equation, (
= 1/((a(2v+b)/T 1/2 2 2 ∂v/∂P) 2 T v (v+b) ) – RT/(v–b) ). As v → ∞, ∂v/∂P= –v 2 /RT.
(d) Therefore using Eq.(d) in Eq.(c), ∂(u o (T) – u(T, v))/
∂P = (3/2)(a/RT 3/2 ).
Rewriting this expression in reduced form and using the RK state equation relation for a =
2 0.4275 R 1.5 T
c /P c , ( ∂u C,R /
∂P 1.5 R ) = 0.6413/T R Using the values for a = 17.39 bar K 1/2 m 6 kmole –2 and R = 0.08314 bar m 3 kmole –1 K –1 for molecular oxygen, at 301 K, ∂(u o (T) – u(T,v))/ ∂P = 0.0601 m 3 kmole –1 or 6.01 kJ kmole -1 bar -1 while the experimental value is given as 0.0651 kmole -1
bar -1 .
Parts
» COMPUTATIONAL MECHANICS and APPLIED ANALYSIS
» Explicit and Implicit Functions and Total Differentiation
» Exact (Perfect) and Inexact (Imperfect) Differentials
» Intermolecular Forces and Potential Energy
» Internal Energy, Temperature, Collision Number and Mean Free Path
» Vector or Cross Product r The area A due to a vector product
» First Law for a Closed System
» First Law For an Open System
» STATEMENTS OF THE SECOND LAW
» Cyclical Integral for a Reversible Heat Engine
» Irreversibility and Entropy of an Isolated System
» Degradation and Quality of Energy
» SINGLE–COMPONENT INCOMPRESSIBLE FLUIDS
» Evaluation of Entropy for a Control Volume
» Internally Reversible Work for an Open System
» MAXIMUM ENTROPY AND MINIMUM ENERGY
» Generalized Derivation for a Single Phase
» LaGrange Multiplier Method for Equilibrium
» Absolute and Relative Availability Under Interactions with Ambient
» Irreversibility or Lost Work
» Applications of the Availability Balance Equation
» Closed System (Non–Flow Systems)
» Heat Pumps and Refrigerators
» Work Producing and Consumption Devices
» Graphical Illustration of Lost, Isentropic, and Optimum Work
» Flow Processes or Heat Exchangers
» CLASSICAL RATIONALE FOR POSTULATORY APPROACH
» Generalized Legendre Transform
» Van der Waals (VW) Equation of State
» Other Two–Parameter Equations of State
» Compressibility Charts (Principle of Corresponding States)
» Boyle Temperature and Boyle Curves
» Three Parameter Equations of State
» Empirical Equations Of State
» State Equations for Liquids/Solids
» Internal Energy (du) Relation
» EXPERIMENTS TO MEASURE (u O – u)
» Vapor Pressure and the Clapeyron Equation
» Saturation Relations with Surface Tension Effects
» Temperature Change During Throttling
» Throttling in Closed Systems
» Procedure for Determining Thermodynamic Properties
» Euler and Gibbs–Duhem Equations
» Relationship Between Molal and Pure Properties
» Relations between Partial Molal and Pure Properties
» Mixing Rules for Equations of State
» Partial Molal Properties Using Mixture State Equations
» Ideal Solution and Raoult’s Law
» Completely Miscible Mixtures
» DEVIATIONS FROM RAOULT’S LAW
» Mathematical Criterion for Stability
» APPLICATION TO BOILING AND CONDENSATION
» Physical Processes and Stability
» Constant Temperature and Volume
» Equivalence Ratio, Stoichiometric Ratio
» Entropy, Gibbs Function, and Gibbs Function of Formation
» Entropy Generated During an Adiabatic Chemical Reaction
» MASS CONSERVATION AND MOLE BALANCE EQUATIONS
» Evaluation of Properties During an Irreversible Chemical Reaction
» Criteria in Terms of Chemical Force Potential
» Generalized Relation for the Chemical Potential
» Nonideal Mixtures and Solutions
» Gas, Liquid and Solid Mixtures
» Availability Balance Equation
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