2 CHAPTER Çengel Boles Thermodynamics Properties of Pure Substances Third Edition WCB/McGraw-Hill © The McGraw-Hill Companies, Inc.,1998 2-1 Constant-Pressure Phase-Change Process (fig. 2-16) Çengel Boles Thermodynamics Third Edition WCB/McGraw-Hill © The McGraw-Hill Companies, Inc.,1998 2-2 T-v Diagram of a Pure Substance Energy, not mass, crosses closed-system boundaries (Fig. 2-18) Çengel Boles Thermodynamics Third Edition WCB/McGraw-Hill © The McGraw-Hill Companies, Inc.,1998 2-3 P-v Diagram of a Pure Substance (Fig. 2-19) Çengel Boles SUPERHEATED Thermodynamics Third Edition WCB/McGraw-Hill © The McGraw-Hill Companies, Inc.,1998 2-4 P-v Diagram of Substance that Contracts on Freezing (Fig. 2-21) Çengel Boles Thermodynamics Third Edition WCB/McGraw-Hill © The McGraw-Hill Companies, Inc.,1998 2-5 P-v Diagram of Substance that Expands on Freezing (Fig. 2-22) Çengel Boles Thermodynamics Third Edition WCB/McGraw-Hill © The McGraw-Hill Companies, Inc.,1998 2-6 P-T Diagram of Pure Substances (Fig. 2-25) Çengel Boles Thermodynamics Third Edition WCB/McGraw-Hill © The McGraw-Hill Companies, Inc.,1998 2-7 P-v-T Surface of a Substance that Contracts on Freezing (Fig. 2-26) Çengel Boles Thermodynamics Third Edition WCB/McGraw-Hill © The McGraw-Hill Companies, Inc.,1998 2-8 P-v-T Surface of a Substance that Expands on Freezing (Fig. 2-27) Çengel Boles Thermodynamics Third Edition WCB/McGraw-Hill © The McGraw-Hill Companies, Inc.,1998 2-9 Partial List of Table A-4 (Fig. 2-35) Çengel Boles Thermodynamics Third Edition WCB/McGraw-Hill © The McGraw-Hill Companies, Inc.,1998 2-10 Quality Shown in P-v and T-v Diagrams Quality is related to the horizontal differences of P-V and T-v diagrams (Fig. 2-41) Çengel Boles Thermodynamics Third Edition WCB/McGraw-Hill © The McGraw-Hill Companies, Inc.,1998 2-11 Partial List of Table A-6 (Fig. 2-45) Çengel Boles Thermodynamics Third Edition WCB/McGraw-Hill © The McGraw-Hill Companies, Inc.,1998 2-12 Pure Substances can Exist as Compressed Liquids At a given P and T, a pure substance will exist as a compressed liquid if T<T sat @ P (Fig. 2-49) Çengel Boles Thermodynamics Third Edition WCB/McGraw-Hill © The McGraw-Hill Companies, Inc.,1998 2-13 The Region Where Steam can be Treated as an Ideal Gas (Fig. 2-54) Çengel Boles Thermodynamics Third Edition WCB/McGraw-Hill © The McGraw-Hill Companies, Inc.,1998 2-14 Comparison of Z Factors for Various Gases (Fig. 2-57) Çengel Boles Thermodynamics Third Edition WCB/McGraw-Hill © The McGraw-Hill Companies, Inc.,1998 2-15 Percent of Error in Equations for the State of Nitrogen (Fig. 2-66) Çengel Boles Thermodynamics Third Edition WCB/McGraw-Hill © The McGraw-Hill Companies, Inc.,1998 2-16 Chapter Summary Çengel Boles Thermodynamics • A substance that has a fixed chemical composition throughout is called a pure substance. Third Edition WCB/McGraw-Hill © The McGraw-Hill Companies, Inc.,1998 2-17 Çengel Boles Chapter Summary Thermodynamics • A pure substance exists in different phases depending on its energy level. In the liquid phase, a substance that is not about to vaporize is called a compressed or subcooled liquid. Third Edition WCB/McGraw-Hill © The McGraw-Hill Companies, Inc.,1998 2-18 Chapter Summary Çengel Boles Thermodynamics • In the gas phase, a substance that is not about to condense is called a superheated vapor. Third Edition WCB/McGraw-Hill © The McGraw-Hill Companies, Inc.,1998 2-19 Çengel Boles Chapter Summary Thermodynamics • During a phase-change process, the temperature and pressure of a pure substance are dependent properties. At a given pressure, a substance changes phase at a fixed temperature, called the saturation temperature. At a given temperature, the pressure at which a substance changes phase is called the saturation pressure. During a boiling process, both the liquid and the vapor phases coexist in equilibrium, and under this condition the liquid is called saturated liquid and the vapor saturated vapor. Third Edition WCB/McGraw-Hill © The McGraw-Hill Companies, Inc.,1998 2-20 Çengel Boles Thermodynamics Third Edition Chapter Summary • In a saturated liquid-vapor mixture, the mass fraction of the vapor phase is called the quality and is defined as The quality may have values between 0 (saturated liquid) and 1 (saturated vapor). It has no meaning in the compressed liquid or superheated vapor regions. WCB/McGraw-Hill © The McGraw-Hill Companies, Inc.,1998 2-21 Çengel Boles Chapter Summary • In the saturated mixture region, the average value of any intensive property y is determined from Thermodynamics where f stands for saturated liquid and g for saturated vapor. Third Edition WCB/McGraw-Hill © The McGraw-Hill Companies, Inc.,1998 2-22 Çengel Boles Chapter Summary Thermodynamics • In the absence of compressed liquid data, a general approximation is to treat a compressed liquid as a saturated liquid at the given temperature, that is, where y stands for v, u, or h. Third Edition WCB/McGraw-Hill © The McGraw-Hill Companies, Inc.,1998 2-23 Çengel Boles Chapter Summary Thermodynamics • The state beyond which there is no distinct vaporization process is called the critical point. At supercritical pressures, a substance gradually and uniformly expands from the liquid to vapor phase. Third Edition WCB/McGraw-Hill © The McGraw-Hill Companies, Inc.,1998 2-24 Çengel Boles Chapter Summary Thermodynamics • All three phases of a substance coexist in equilibrium at states along the triple line characterized by triple-line temperature and pressure. Third Edition WCB/McGraw-Hill © The McGraw-Hill Companies, Inc.,1998 2-25 Çengel Boles Chapter Summary Thermodynamics • Various properties of some pure sub-stances are listed in the appendix. As can be noticed from these tables, the compressed liquid has lower v, u, and h values than the saturated liquid at the same T or P. Likewise, superheated vapor has higher v, u, and h values than the saturated vapor at the same T or P. is a major application area of thermodynamics. Third Edition WCB/McGraw-Hill © The McGraw-Hill Companies, Inc.,1998 2-26 Çengel Boles Chapter Summary Thermodynamics • Any relation among the pressure, temperature, and specific volume of a substance is called an equation of state. The simplest and best-known equation of state is the ideal-gas equation of state, given as where R is the gas constant. Caution should be exercised in using this relation since an ideal gas is a fictitious substance. Real gases exhibit idealgas behav-ior at relatively low pressures and high temperatures. Third Edition WCB/McGraw-Hill © The McGraw-Hill Companies, Inc.,1998 2-27 Çengel Boles Chapter Summary Thermodynamics • The deviation from ideal-gas behavior can be properly accounted for by using the compressibility factor Z, defined as Third Edition WCB/McGraw-Hill © The McGraw-Hill Companies, Inc.,1998 2-28 Çengel Boles Chapter Summary Thermodynamics • The Z factor is approximately the same for all gases at the same reduced temperature and reduced pressure, which are defined as where Pcr and Tcr are the critical pressure and temperature, respectively. This is known as the principle of corresponding states. Third Edition (Continued on next slide) WCB/McGraw-Hill © The McGraw-Hill Companies, Inc.,1998 2-29 Chapter Summary (Continued from previous slide) Çengel Boles Thermodynamics • When either P or T is unknown, Z can be determined from the compressibility chart with the help of the pseudo-reduced specific volume, defined as Third Edition WCB/McGraw-Hill © The McGraw-Hill Companies, Inc.,1998 2-30 Chapter Summary • The P-v-T behavior of substances can be represented more accurately by the more complex equations of state. Three of the best known are Çengel Boles Thermodynamics van der Waals: where Third Edition WCB/McGraw-Hill © The McGraw-Hill Companies, Inc.,1998 2-31 Chapter Summary • Beattie-Bridgeman: Çengel Boles Thermodynamics where Third Edition WCB/McGraw-Hill © The McGraw-Hill Companies, Inc.,1998 2-32 Çengel Boles Chapter Summary • Benedict-Webb-Rubin: Thermodynamics Third Edition The constants appearing in the Beattie-Bridgeman and Benedict-WebbRubin equations are given in Table A-29 for various substances. WCB/McGraw-Hill © The McGraw-Hill Companies, Inc.,1998