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CEN 202

CHAPTER 4. EFFECTS

TEXT BOOK: : J. M. SMITH, H. C. VAN NESS, M. M. ABBOTT, M. T. SWIHART. “INTRODUCTION TO CHEMICAL ENGINEERING THERMODYNAMICS”, EIGHTH EDITION. 2018 CEN 202 THERMODYNAMICS, HEAT EFFECTS

Heat effects refer to physical and chemical phenomena that are associated with to or from a system or that result in temperature changes within a system, or both.

Latent heat: is related to changes in between liquids, gases, and solids (at constant T and P).

Chemical reactions are characterised by of reaction ( reactions evolve heat, for example). Every chemical or biochemical process is associated with one or more heat effects.

Text Book: : J. M. Smith, H. C. Van Ness, M. M. Abbott, M. T. Swihart. “INTRODUCTION TO CHEMICAL ENGINEERING THERMODYNAMICS”, EIGHTH EDITION. 2018 SENSIBLE HEAT EFFECTS

• Heat transfer to or from a system in which there are no phase transitions, no chemical reactions, and no changes in composition causes a “sensible heat effect”, i.e., the temperature of the system is caused to change.

• Briefly, sensible heat is related to changes in temperature of a gas or object with no change in phase. • A relation between; the quantity of heat transferred ↔ the resulting temperature change.

Text Book: : J. M. Smith, H. C. Van Ness, M. M. Abbott, M. T. Swihart. “INTRODUCTION TO CHEMICAL ENGINEERING THERMODYNAMICS”, EIGHTH EDITION. 2018 SENSIBLE HEAT EFFECTS • U (molar or specific) = U (T, V). Then,

흏푼 흏푼 • 풅푼 = 풅푻 + 풅푽 흏푻 푽 흏푽 푻 푪푽

흏푼 • 풅푼 = 푪푽풅푻 + 풅푽 흏푽 푻 =ퟎ • For any closed-system constant- process. • Whenever the is independent of volume, as for the ideal-gas state and the incompressible liquid.

푻ퟐ In either case, 풅푼 = 푪푽풅푻 and ∆푼 = ׬ 푪푽풅푻 • 푻ퟏ Text Book: : J. M. Smith, H. C. Van Ness, M. M. Abbott, M. T. Swihart. “INTRODUCTION TO CHEMICAL ENGINEERING THERMODYNAMICS”, EIGHTH EDITION. 2018 SENSIBLE HEAT EFFECTS • For ; • H (molar or specific) = H (T, P). Then,

흏푯 흏푯 • 풅푯 = 풅푻 + 풅푷 흏푻 푷 흏푷 푻 푪푷

흏푯 • 풅푯 = 푪푷풅푻 + 풅푷 흏푷 푻 =ퟎ The final term is zero in two circumstances: • For any constant- process. • When the enthalpy is independent of pressure, regardless of process. This is exactly true for the ideal-gas state and approximately true for real gases at low pressure and high temperature.

푻ퟐ In either case, 풅푯 = 푪푷풅푻 and ∆푯 = ׬ 푪푷풅푻 • 푻ퟏ

Text Book: : J. M. Smith, H. C. Van Ness, M. M. Abbott, M. T. Swihart. “INTRODUCTION TO CHEMICAL ENGINEERING THERMODYNAMICS”, EIGHTH EDITION. 2018 TEMPERATURE DEPENDENCE OF THE

푻ퟐ Evaluation of the integral in Eq. 푸 = ∆푯 = ׬ 푪푷풅푻 requires knowledge of the • 푻ퟏ temperature dependence of the heat capacity. This is usually given by an empirical equation; the two simplest expressions of practical value are: 푪 푪 푷 = 휶 + 휷푻 + 휸푻ퟐ 풂풏풅 푷 = 풂 + 풃푻 + 풄푻−ퟐ 푹 푹 where α, β, and γ and a, b, and c are constants characteristic of the particular substance. With the exception of the last term, these equations are of the same form. We therefore combine them to provide a single expression:

푪 푷 = 푨 + 푩푻 + 푪푻ퟐ + 푫푻−ퟐ 푹 where either C or D is usually zero, depending on the substance considered. Because the ratio CP/R is dimensionless, the units of CP are governed by the choice of R. The parameters are independent of temperature, but, at least in principle, depend on the value of the constant pressure.

Text Book: : J. M. Smith, H. C. Van Ness, M. M. Abbott, M. T. Swihart. “INTRODUCTION TO CHEMICAL ENGINEERING THERMODYNAMICS”, EIGHTH EDITION. 2018 HEAT CAPACITY IN THE IDEAL-GAS STATE Temperature dependence is expressed analytically (for ): 퐢퐠 퐂 퐏 = 퐀 + 퐁퐓 + 퐂퐓ퟐ + 퐃퐓−ퟐ 퐑 Values of the constants are given in Tables (Table C.1 of App. C for a number of common organic and inorganic gases) in available literature.

The two ideal-gas-state heat capacities are related: (remember: CP=CV+R) 푪풊품 푪풊품 푽 = 푷 − ퟏ 푹 푹 풊품 푪 The temperature dependence of 푽 follows from the temperature dependence 푹 풊품 푪 of 푷 . 푹

Text Book: : J. M. Smith, H. C. Van Ness, M. M. Abbott, M. T. Swihart. “INTRODUCTION TO CHEMICAL ENGINEERING THERMODYNAMICS”, EIGHTH EDITION. 2018