Fundamentals of Thermodynamics Chapter 2 Pure Substance Behavior Prof. Siyoung Jeong Thermodynamics I MEE2022-02 Spring 2014 Chapter 2. Pure Substance Behavior 2.1 The pure substance • Pure substance - Homogeneous, invariable chemical composition • Liquid air : 2 components, 2 phase • Simple compressible - Surface, magnetic, electrical effects : negligible - Volume change : important Thermal Engineering Lab. 2 Chapter 2. Pure Substance Behavior 2.2 The phase boundaries Thermal Engineering Lab. 3 Chapter 2. Pure Substance Behavior • Triple point : Table 2.1 • Critical point: Table 2.2 Thermal Engineering Lab. 4 Chapter 2. Pure Substance Behavior Thermal Engineering Lab. 5 Chapter 2. Pure Substance Behavior 2.3 The P-v-T surface Thermal Engineering Lab. 6 Chapter 2. Pure Substance Behavior Thermal Engineering Lab. 7 Chapter 2. Pure Substance Behavior Thermal Engineering Lab. 8 Chapter 2. Pure Substance Behavior • Independent properties of a pure substance - Simple compressible pure substance : absence of motion, gravity, surface, magnetic, electrical effects - Defined by 2 independent properties • Saturated liquid와 saturated vapor는 state가 다르지만 동일한 P, T • → Saturated state에서는 P, T 는 서로 dependent Subcooled (compressed) liquid : P, v, T 중 어느 2가지로 상태 결정 가능 → (P, v) , (P, T) • Saturated state : (P, T)는 dependent 이기 때문에 상태 결정 불가능 → (P, v) , (v, T) 가능 → (T, x) , (P, x) 가능 Thermal Engineering Lab. 9 Chapter 2. Pure Substance Behavior 2.4 Tables of thermodynamics properties V Vg V f mv mg v g m f v f v xv g (1 x)v f v f xv fg Thermal Engineering Lab. 10 Chapter 2. Pure Substance Behavior Ex. 2.1 Determine the phase for each of the following water states using the tables in Appendix B and indicate the relative position in the P-v, T-v, and P-T diagrams. a. 120℃, 500 kPa b. 120℃, 0.5 m3/kg Thermal Engineering Lab. 11 Chapter 2. Pure Substance Behavior • 낮은 압력에서 가열하는 경우 (A-B) : • • • solid → vapor 삼중점보다 높은 압력에서 가열하는 경우 (E-F) : solid → liquid → vapor 특정 압력 (0.6113 kPa)에서 가열하는 경우 (C-D) : → Triple point 통과 임계점 이상의 압력에서 가열하는 경우 (G-H) : → 뚜렷한 상변화 없이 상태 변화 Thermal Engineering Lab. 12 Chapter 2. Pure Substance Behavior 2.5 The two-phase states Vapor Quality Liquid Vapor x mg m , 1 x mf m V Vliq Vvap mliqv f mvapvg v mvap V mliq vf v g (1 x)v f xv g m m m With v fg v g v f , v v f xv fg x Thermal Engineering Lab. v vf v fg 13 Chapter 2. Pure Substance Behavior Ex. 2.2 A closed vessel contains 0.1 m3 of saturated liquid and 0.9 m3 of saturated vapor R-134a in equilibrium at 30℃. Determine the percent vapor on a mass basis. Thermal Engineering Lab. 14 Chapter 2. Pure Substance Behavior 2.6 The liquid and solid states • Compressed liquid (Subcooled liquid) - Liquid that has a pressure higher than the saturation pressure for a given temperature - Temperature is lower than the saturation temperature (at the same saturation pressure above) - Specific volume is a weak function of temperature (incompressible) v v(T ) v f • Compressed solid (Subcooled solid) - A state with a temperature lower than the saturated temperature for a given pressure on the fusion (sublimination) line - Specific volume is a weak function of temperature (incompressible) v v(T ) vi Thermal Engineering Lab. 15 Chapter 2. Pure Substance Behavior 2.7 The superheated vapor states - A state with a pressure lower than the saturated pressure for given temperature - Higher temperature than the saturated temperature (at the same saturated pressure above) Thermal Engineering Lab. 16 Chapter 2. Pure Substance Behavior Ex. 2.3 Determine the phase for each of the following states using the tables in Appendix B and indicate the relative position in the P-v, T-v, and P-T diagrams, as in Fig. 2.11. a. Ammonia 30℃, 1000 kPa b. R-134a 200 kPa, 0.125 m3/kg Thermal Engineering Lab. 17 Chapter 2. Pure Substance Behavior Ex. 2.4 A rigid vessel contains saturate ammonia vapor at 20℃. Heat is transferred to the system until the temperature reaches 40℃. What is the final pressure? Thermal Engineering Lab. 18 Chapter 2. Pure Substance Behavior Ex. 2.5 Determine the pressure for water at 200℃ with v = 0.4 m3/kg. Thermal Engineering Lab. 19 Chapter 2. Pure Substance Behavior 2.8 The ideal gas states Pv RT R kJ R , R 8.3145 M kmol K n m M PV mRT nR T Thermal Engineering Lab. 20 Chapter 2. Pure Substance Behavior Ex. 2.6 What is the mass of air contained in a room 6 m × 10 m × 4 m if the pressure is 100 kPa and the temperature is 25℃? Thermal Engineering Lab. 21 Chapter 2. Pure Substance Behavior Ex. 2.7 A tank has a volume of 0.5 m3 and contains 10 kg of an ideal gas having a molecular mass of 24. The temperature is 25℃. What is the pressure? Thermal Engineering Lab. 22 Chapter 2. Pure Substance Behavior Ex. 2.8 A gas bell is submerged in liquid water, with its mass counterbalanced with rope and pulleys, as shown in Fig. 2.18. The pressure inside is measured carefully to be 105 kPa, and the temperature is 21℃. A volume increase is measured to be 0.75 m3 over a period of 185 s. What is the volume flow rate and the mass flow rate of the flow into the bell, assuming it is carbon dioxide gas? Thermal Engineering Lab. 23 Chapter 2. Pure Substance Behavior Thermal Engineering Lab. 24 Chapter 2. Pure Substance Behavior 2.9 The compressibility factor Pv Z , Pv ZRT RT Z • vactual videal T P v , Pr , vr Reduced property : Tr Tc Pc vc • Generalized compressibility chart T P Tr , Pr Tc Pc → Generalized chart Thermal Engineering Lab. 25 Chapter 2. Pure Substance Behavior Thermal Engineering Lab. 26 Chapter 2. Pure Substance Behavior Ex. 2.9 Is it reasonable to assume ideal gas behavior at each of the given states? a. Nitrogen at 20℃, 1.0 MPa b. Carbon dioxide at 20℃, 1.0 MPa c. Ammonia at 20℃, 1.0 MPa Thermal Engineering Lab. 27 Chapter 2. Pure Substance Behavior Ex. 2.10 Determine the specific volume for R-134a at 100℃, 3.0 MPa for the following models: a. The R-134a tables, Table B.5 b. Ideal gas c. The generalized chart, Fig. D.1 Thermal Engineering Lab. 28 Chapter 2. Pure Substance Behavior Ex. 2.11 Propane in a steel bottle of volume 0.1 m3 has a quality 10% at a temperature of 15℃. Use the generalized compressibility chart to estimate the total propane mass and to find the pressure. Thermal Engineering Lab. 29 Chapter 2. Pure Substance Behavior 2.10 Equations of state RT a P 2 v b v cbv db 2 RT a P 2 v b v : Cubic equation of state : Van der Waals equation Thermal Engineering Lab. 30 Chapter 2. Pure Substance Behavior 2.11 Computerized tables Thermal Engineering Lab. 31 Chapter 2. Pure Substance Behavior 2.12 Engineering applications Thermal Engineering Lab. 32
© Copyright 2026 Paperzz