chapter 4 atkins pchem
TRANSCRIPT
-
8/13/2019 Chapter 4 atkins pchem
1/57
Physical
Transformations ofPure Substances
Chapter 4
-
8/13/2019 Chapter 4 atkins pchem
2/57
Definitions
!A phase is a state of matter that is uniformthroughout, not only in composition but also in
physical state.
!A pure gas!A gaseous mixture!Two totally miscible liquids!A crystal
-
8/13/2019 Chapter 4 atkins pchem
3/57
Definitions
!A solution of sodium chloride! Ice!A slurry of ice and water
-
8/13/2019 Chapter 4 atkins pchem
4/57
Definitions
!An alloy of two metals?
-
8/13/2019 Chapter 4 atkins pchem
5/57
-
8/13/2019 Chapter 4 atkins pchem
6/57
Definitions
!An alloy of two metals is a two phase system ifthe metals are immiscible, but a single phase
system if they are miscible.
! Dispersion can be uniform on a macroscopiclevel, but not on a microscopic scale.
! Dispersions are important in many advancedmaterials.
-
8/13/2019 Chapter 4 atkins pchem
7/57
-
8/13/2019 Chapter 4 atkins pchem
8/57
Stabilities of Phase! A phase of a substance is a form of matter that is
uniform throughout in chemical composition and
physical state.
! A phase transition is the spontaneous conversion ofone phase into another.
! Phase transitions occur at a characteristictemperature and pressure.
-
8/13/2019 Chapter 4 atkins pchem
9/57
Stabilities of Phase! At 1 atm, < 0 C, ice is the stable phase of H2O,
but > 0 C, liquid water is the stable phase.
!The transition temperature, Ttrs, is the temperatureat which two phases are in equilibrium.
! So what happens to Gibbs energy?
-
8/13/2019 Chapter 4 atkins pchem
10/57
Stabilities of Phase! At 1 atm, < 0 C, ice is the stable phase of H2O,
but > 0 C, liquid water is the stable phase.
!The transition temperature, Ttrs, is the temperatureat which two phases are in equilibrium.
! So what happens to Gibbs energy?! < 0 C Gibbs energy decreases as liquid"solid.! > 0 C Gibbs energy decreases as solid"liquid.
-
8/13/2019 Chapter 4 atkins pchem
11/57
Stabilities of Phase
-
8/13/2019 Chapter 4 atkins pchem
12/57
Phase Diagrams
-
8/13/2019 Chapter 4 atkins pchem
13/57
Vapor Pressure
-
8/13/2019 Chapter 4 atkins pchem
14/57
Boiling Point
-
8/13/2019 Chapter 4 atkins pchem
15/57
Critical Point
-
8/13/2019 Chapter 4 atkins pchem
16/57
Critical Point
-
8/13/2019 Chapter 4 atkins pchem
17/57
Melting and Freezing
-
8/13/2019 Chapter 4 atkins pchem
18/57
-
8/13/2019 Chapter 4 atkins pchem
19/57
Triple Point
-
8/13/2019 Chapter 4 atkins pchem
20/57
Carbon Dioxide
-
8/13/2019 Chapter 4 atkins pchem
21/57
-
8/13/2019 Chapter 4 atkins pchem
22/57
Helium
-
8/13/2019 Chapter 4 atkins pchem
23/57
Definitions
!A constituent of a system is a chemical species(an ion or a molecule) that is present.
!A mixture of water and ethanol has twoconstituents.
!A solution of sodium chloride has threeconstituents: Na+, Cl-, H2O.
-
8/13/2019 Chapter 4 atkins pchem
24/57
Definitions
!A component is a chemically independentconstituent of a system.
!The number of components in a system is theminimum number of independent species
necessary to define the composition of all the
phases present in the system.
-
8/13/2019 Chapter 4 atkins pchem
25/57
Definitions
!When no reaction takes place and there are noother constraints, the number of components is
the equal to the number of constituents.
! Pure water is a one component system!A mixture of ethanol and water is two
component system.
-
8/13/2019 Chapter 4 atkins pchem
26/57
Definitions
!An aqueous solution of sodium chloride is a twocomponent system, because by charge balance,
the number of Na+ions must be the same as the
number of Cl-ions.
!A system that consists of hydrogen, oxygen andwater at room temperature has three
components.
-
8/13/2019 Chapter 4 atkins pchem
27/57
Definitions
!The number of phases, P.!The number of components, C.!The variance of the system, F is the number of
intensive variables (e.g. p and T) that can be
changed independently without disturbing the
number of phases in equilibrium.
-
8/13/2019 Chapter 4 atkins pchem
28/57
Phase Rule
! F = C P + 2!This is not an empirical rule based upon
observations, it can be derived from chemicalthermodynamics.
! For a one component system F = 3 P!When only one phase is present, F = 2 and both
p and T can be varied without changing the
number of phases.
-
8/13/2019 Chapter 4 atkins pchem
29/57
-
8/13/2019 Chapter 4 atkins pchem
30/57
-
8/13/2019 Chapter 4 atkins pchem
31/57
Experimental Procedures
!Thermal analysis a sample is allowed to cooland it temperature is monitored. When a phase
transition occurs, cooling may stop until the
phase transition is complete and is easily
observed on a thermogram.
-
8/13/2019 Chapter 4 atkins pchem
32/57
-
8/13/2019 Chapter 4 atkins pchem
33/57
Experimental Procedures
! Modern work on phase transitions often dealwith systems at very high pressures and more
sophisticated detection properties must be
adopted.
!A diamond anvil cell is capable of producingextremely high pressures.
-
8/13/2019 Chapter 4 atkins pchem
34/57
Experimental Procedures
!A sample is placed in a cavity between to gem-quality diamonds and then pressure is exerted by
turning a screw. Pressures up to ~2 Mbar can be
achieved.
! One application is the study the transition ofcovalent solids to metallic solids.
-
8/13/2019 Chapter 4 atkins pchem
35/57
-
8/13/2019 Chapter 4 atkins pchem
36/57
Experimental Procedures
! Iodine, I2, becomes metallic at ~ 200 kbar andmakes a transition to a monatomic metallic solid
at around 210 kbar.
! Relevant to the structure of material deep insidethe Earth and in the interiors of giant planets,
where even hydrogen may be metallic.
-
8/13/2019 Chapter 4 atkins pchem
37/57
Thermodynamics of Phase
Transitions
-
8/13/2019 Chapter 4 atkins pchem
38/57
Thermodynamics of Phase
Transitions
-
8/13/2019 Chapter 4 atkins pchem
39/57
Thermodynamics of Phase
Transitions
-
8/13/2019 Chapter 4 atkins pchem
40/57
Temperature Dependence of
Phase Transitions
"Gm
"T
#
$%
&
'(p
=)Sm"
"T
#
$%
&
'(p
=)Sm
-
8/13/2019 Chapter 4 atkins pchem
41/57
Melting and Applied Pressure
"Gm
"p
#
$%
&
'(T
=Vm"
"p
#
$%
&
'(T
=Vm
-
8/13/2019 Chapter 4 atkins pchem
42/57
Melting and Applied Pressure
"Gm
"p
#
$%
&
'(T
=Vm"
"p
#
$%
&
'(T
=Vm
-
8/13/2019 Chapter 4 atkins pchem
43/57
Vapor Pressure and Applied
Pressure
p = p*eVm ( l )"P RT
p = vapor pressure
p
*=
vapor pressure of condensed phasein the absence of an additional pressure
"P = pressure applied
-
8/13/2019 Chapter 4 atkins pchem
44/57
Vapor Pressure and Applied
Pressure
-
8/13/2019 Chapter 4 atkins pchem
45/57
Location of Phase Boundaries
"(p,T) = #(p,T)
-
8/13/2019 Chapter 4 atkins pchem
46/57
Location of Phase Boundaries
dG =Vdp" SdT
d=Vmdp " SmdT
V#,mdp" S#,mdT=V$,mdp" S$,mdT
(S$,m " S#,m )dT=(V$,m "V#,m )dp
%trs
S
% trsV=
dp
dT "Clapeyron equation
-
8/13/2019 Chapter 4 atkins pchem
47/57
Location of Phase Boundaries
-
8/13/2019 Chapter 4 atkins pchem
48/57
Solid-liquid boundary
" trsS
" trsV=
dp
dT#Clapeyron equation
" trsS= "trsHT
dp
dT
=
" fusH
T" fusV
-
8/13/2019 Chapter 4 atkins pchem
49/57
Solid-liquid boundary
-
8/13/2019 Chapter 4 atkins pchem
50/57
Solid-liquid boundary
dpdT
= " fusHT" fusV
dp =" fusH
" fusV
dT
T
dp =" fusH
" fusV
dT
TT*
T
#p
*
p
#
dp$" fusH
" trsV
dT
TT
*
T
#p
*
p
#
p$ p* +" fusH
" fusVln
T
T*
%
&'
(
)*
-
8/13/2019 Chapter 4 atkins pchem
51/57
Solid-liquid boundary
p" p* +# fusH
# fusVln
T
T*
$
%&
'
()
When T and T*
do not differ much
p" p* +# fusH
T*# fusV
(T* T*)
-
8/13/2019 Chapter 4 atkins pchem
52/57
Liquid-vapor boundary
" trsS
" trsV=
dp
dT#Clapeyron equation
" trsS= "trsHT
dp
dT
=
" vapH
T" vapV
-
8/13/2019 Chapter 4 atkins pchem
53/57
Liquid-vapor boundary
dp
dT
" "small"
dT
dp" "large"
-
8/13/2019 Chapter 4 atkins pchem
54/57
Liquid-vapor boundary
dp
dT=
" vapH
T" vapV" vapV # Vm (g)
dp
dT=
" vapH
T(RT p)
dlnp
dT
=
" vapH
RT2
- Clausius - Clapeyron equation
-
8/13/2019 Chapter 4 atkins pchem
55/57
Liquid-vapor boundarydlnp
dT=
" vapH
RT2
dlnp =" vapH
RT2
dT
dlnpln p *
ln p
# =" vapH
RT2
dTT*
T
#
dlnpln p *
ln p# = " vapHR
dTT
2T*
T# =$"vapHR
1
T$ 1
T*
%
&' (
)*
ln p p*( ) =$
"vapH
R
1
T$ 1
T*
%
&'
(
)*
p
p*=e
$+
+=
" vapH
R
1
T$
1
T*
%
&'
(
)*
p = p*e$+
-
8/13/2019 Chapter 4 atkins pchem
56/57
Liquid-vapor boundarydlnp
dT=
" vapH
RT2
dlnp =" vapH
RT2
dT
dlnpln p *
ln p
# =" vapH
RT2
dTT*
T
#
dlnpln p *
ln p# = " vapHR
dTT
2T*
T# =$"vapHR
1
T$ 1
T*
%
&' (
)*
ln p p*( ) =$
"vapH
R
1
T$ 1
T*
%
&'
(
)*
p
p*=e
$++=
" vapH
R
1
T$
1
T*
%
&'
(
)*
p = p*e$+
-
8/13/2019 Chapter 4 atkins pchem
57/57
Solid-gas boundary
p = p*e"#
#=$ subH
R
1
T" 1
T*
%
&'
(
)*