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CHAPTER
                       15

Chemical and Phase
Equilibrium
Copyright © The McGraw-Hill Companies, Inc. Permission required for reproduction or display.


FIGURE 15-1
A reaction
chamber that
contains a
mixture of CO2,
CO, and O2 at a
specified
temperature and
pressure.




15-1
Copyright © The McGraw-Hill Companies, Inc. Permission required for reproduction or display.


FIGURE 15-2
Equilibrium criteria
for a chemical
reaction that takes
place adiabatically.




15-2
Copyright © The McGraw-Hill Companies, Inc. Permission required for reproduction or display.

FIGURE 15-3
A control mass
undergoing a chemical
reaction at a specified
temperature and
pressure.




15-3
Copyright © The McGraw-Hill Companies, Inc. Permission required for reproduction or display.

FIGURE 15-4
Criteria for chemical
equilibrium at a
specified temperature
and pressure.




15-4
Copyright © The McGraw-Hill Companies, Inc. Permission required for reproduction or display.


FIGURE 15-5
An infinitesimal reaction in a
chamber at constant temperature
and pressure.




15-5
Copyright © The McGraw-Hill Companies, Inc. Permission required for reproduction or display.


FIGURE 15-7
Three equivalent Kp relations
for reacting ideal-gas mixtures.




15-6
Copyright © The McGraw-Hill Companies, Inc. Permission required for reproduction or display.


FIGURE 15-9
The larger the KP,
the more complete
the reaction.




15-7
Copyright © The McGraw-Hill Companies, Inc. Permission required for reproduction or display.


FIGURE 15-10
The presence of inert
gases does not affect
the equilibrium
constant, but it does
affect the equilibrium
composition.




15-8
Copyright © The McGraw-Hill Companies, Inc. Permission required for reproduction or display.


FIGURE 15-11
Equilibrium-constant
relation for the
ionization reaction of
hydrogen.




15-9
Copyright © The McGraw-Hill Companies, Inc. Permission required for reproduction or display.


FIGURE 15-14
The number of KP relations needed to
determine the equilibrium
composition of a reacting mixture is
the difference between the number of
species and the number of elements.




15-10
Copyright © The McGraw-Hill Companies, Inc. Permission required for reproduction or display.


FIGURE 15-16
Exothermic
reactions are less
complete at higher
temperatures.




15-11
Copyright © The McGraw-Hill Companies, Inc. Permission required for reproduction or display.


FIGURE 15-18
A liquid–vapor mixture in
equilibrium at a constant
temperature and pressure.




15-12
Copyright © The McGraw-Hill Companies, Inc. Permission required for reproduction or display.


FIGURE 15-20
A multicomponent
multiphase system is in
phase equilibrium when
the specific Gibbs
function of each
component is the same in
all phases.




15-13
Copyright © The McGraw-Hill Companies, Inc. Permission required for reproduction or display.


FIGURE 15-21
Equilibrium
diagram for the
two-phase mixture
of oxygen and
nitrogen at 0.1 MPa.




15-14
Copyright © The McGraw-Hill Companies, Inc. Permission required for reproduction or display.


FIGURE 15-22
Unlike temperature,
the mole fraction of
species on the two
sides of a liquid–gas
(or solid–gas or
solid–liquid)
interface are usually
not the same.




15-15
Copyright © The McGraw-Hill Companies, Inc. Permission required for reproduction or display.


FIGURE 15-23
Dissolved gases in a
liquid can be driven
off by heating the
liquid.




15-16

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  • 1. CHAPTER 15 Chemical and Phase Equilibrium
  • 2. Copyright © The McGraw-Hill Companies, Inc. Permission required for reproduction or display. FIGURE 15-1 A reaction chamber that contains a mixture of CO2, CO, and O2 at a specified temperature and pressure. 15-1
  • 3. Copyright © The McGraw-Hill Companies, Inc. Permission required for reproduction or display. FIGURE 15-2 Equilibrium criteria for a chemical reaction that takes place adiabatically. 15-2
  • 4. Copyright © The McGraw-Hill Companies, Inc. Permission required for reproduction or display. FIGURE 15-3 A control mass undergoing a chemical reaction at a specified temperature and pressure. 15-3
  • 5. Copyright © The McGraw-Hill Companies, Inc. Permission required for reproduction or display. FIGURE 15-4 Criteria for chemical equilibrium at a specified temperature and pressure. 15-4
  • 6. Copyright © The McGraw-Hill Companies, Inc. Permission required for reproduction or display. FIGURE 15-5 An infinitesimal reaction in a chamber at constant temperature and pressure. 15-5
  • 7. Copyright © The McGraw-Hill Companies, Inc. Permission required for reproduction or display. FIGURE 15-7 Three equivalent Kp relations for reacting ideal-gas mixtures. 15-6
  • 8. Copyright © The McGraw-Hill Companies, Inc. Permission required for reproduction or display. FIGURE 15-9 The larger the KP, the more complete the reaction. 15-7
  • 9. Copyright © The McGraw-Hill Companies, Inc. Permission required for reproduction or display. FIGURE 15-10 The presence of inert gases does not affect the equilibrium constant, but it does affect the equilibrium composition. 15-8
  • 10. Copyright © The McGraw-Hill Companies, Inc. Permission required for reproduction or display. FIGURE 15-11 Equilibrium-constant relation for the ionization reaction of hydrogen. 15-9
  • 11. Copyright © The McGraw-Hill Companies, Inc. Permission required for reproduction or display. FIGURE 15-14 The number of KP relations needed to determine the equilibrium composition of a reacting mixture is the difference between the number of species and the number of elements. 15-10
  • 12. Copyright © The McGraw-Hill Companies, Inc. Permission required for reproduction or display. FIGURE 15-16 Exothermic reactions are less complete at higher temperatures. 15-11
  • 13. Copyright © The McGraw-Hill Companies, Inc. Permission required for reproduction or display. FIGURE 15-18 A liquid–vapor mixture in equilibrium at a constant temperature and pressure. 15-12
  • 14. Copyright © The McGraw-Hill Companies, Inc. Permission required for reproduction or display. FIGURE 15-20 A multicomponent multiphase system is in phase equilibrium when the specific Gibbs function of each component is the same in all phases. 15-13
  • 15. Copyright © The McGraw-Hill Companies, Inc. Permission required for reproduction or display. FIGURE 15-21 Equilibrium diagram for the two-phase mixture of oxygen and nitrogen at 0.1 MPa. 15-14
  • 16. Copyright © The McGraw-Hill Companies, Inc. Permission required for reproduction or display. FIGURE 15-22 Unlike temperature, the mole fraction of species on the two sides of a liquid–gas (or solid–gas or solid–liquid) interface are usually not the same. 15-15
  • 17. Copyright © The McGraw-Hill Companies, Inc. Permission required for reproduction or display. FIGURE 15-23 Dissolved gases in a liquid can be driven off by heating the liquid. 15-16