Title: Group B
1Group B
- Topics
- Saturation Vapor Pressure as a Problem of
Equilibrium - Solute and Curvature Effects as Applied to a
Kohler Curve
2Saturation Vapor Pressure as a Problem of
Equilibrium
- Learning Goals
- The student should be able to define
- Vapor Pressure
- Saturation Vapor Pressure
- Equilibrium
- Relative Humidity
3Saturation Vapor Pressure as a Problem of
Equilibrium
- Learning Goals
- The student should be able to
- Describe the effect of salinity on saturation
- Describe the effect of temperature on saturation
- Describe the effect of total ambient air pressure
on saturation
4Saturation Vapor Pressure as a Problem of
Equilibrium
- Learning Goals
- The student should be able to
- Describe the effect of salinity on freezing and
boiling point - Describe the effect of vapor pressure and
saturation vapor pressure on relative humidity
5Saturation Vapor Pressure as a Problem of
Equilibrium
- Teaching Strategy
- Lecture
- Exploratory
6Saturation Vapor Pressure as a Problem of
Equilibrium
- Teaching Strategy
- Lecture
- Discussion of Learning Objective Content
- Power Point Lecture
- Exploratory
- Java Applet
- Active Learning
- In Class Exercise
- Homework
7Saturation Vapor Pressure as a Problem of
Equilibrium
- Teaching Strategy
- Exploratory
- Java Applet
- Variables
- Temperature
- Salinity
- Total Ambient Pressure
8Saturation Vapor Pressure as a Problem of
Equilibrium
- Teaching Strategy
- Exploratory
- Java Applet
- Output
- Rate of Evaporation
- Rate of Condensation
- Actual Vapor Pressure
- Saturation Vapor Pressure
- Relative Humidity
9Saturation Vapor Pressure as a Problem of
Equilibrium
- Teaching Strategy
- Exploratory
- Java Applet
- Output
- Dew Point
- Boiling Point
- Freezing Point
10Dry Air
Saturation Vapor Pressure (mb)
Tw 0ºC
Rate of Evaporation and Condensation (kg m-2 s-1)
-50
0
50
0
50
100
CLEAR
CLEAR
Time (s)
Temperature (C)
Evaporation
Condensation
WRT Liquid
WRT Ice
Equilibrium
Freezing Point
Temperature (C)
RUN
Pressure Units
Pressure
Atm
-50
50
0
1013.15
PAUSE
Salinity ( seawater)
mb
X
in Hg
Boiling Point 100.0C Freezing Point 0.0C
0
100
50
mm Hg (torr)
11Dry Air
Tw 15ºC
Saturation Vapor Pressure (mb)
Rate of Evaporation and Condensation (kg m-2 s-1)
-50
0
50
0
50
100
CLEAR
CLEAR
Time (s)
Temperature (C)
Evaporation
Condensation
WRT Liquid
WRT Ice
Equilibrium
Freezing Point
Temperature (C)
RUN
Pressure Units
Pressure
Atm
-50
50
0
1013.15
PAUSE
Salinity ( seawater)
mb
X
in Hg
Boiling Point 100.0C Freezing Point 0.0C
0
100
50
mm Hg (torr)
12Dry Air
Tw 15ºC
Saturation Vapor Pressure (mb)
Rate of Evaporation and Condensation (kg m-2 s-1)
-50
0
50
0
50
100
CLEAR
CLEAR
Time (s)
Temperature (C)
Evaporation
Condensation
WRT Liquid
WRT Ice
Equilibrium
Freezing Point
Temperature (C)
RUN
Pressure Units
Pressure
Atm
-50
50
0
1013.15
PAUSE
Salinity ( seawater)
mb
X
in Hg
Boiling Point 101.5C Freezing Point -0.5C
0
100
50
mm Hg (torr)
13Tw 15ºC
Saturation Vapor Pressure (mb)
Rate of Evaporation and Condensation (kg m-2 s-1)
-50
0
50
0
50
100
CLEAR
CLEAR
Time (s)
Temperature (C)
Evaporation
Condensation
WRT Liquid
WRT Ice
Equilibrium
Freezing Point
Temperature (C)
RUN
Pressure Units
Pressure
Atm
-50
50
0
1013.15
PAUSE
Salinity ( seawater)
mb
X
in Hg
Boiling Point 101.5C Freezing Point -0.5C
0
100
50
mm Hg (torr)
14Tw 15ºC
Saturation Vapor Pressure (mb)
Rate of Evaporation and Condensation (kg m-2 s-1)
-50
0
50
0
50
100
CLEAR
CLEAR
Time (s)
Temperature (C)
Evaporation
Condensation
WRT Liquid
WRT Ice
Equilibrium
Freezing Point
Temperature (C)
RUN
Pressure Units
Pressure
Atm
-50
50
0
1013.15
PAUSE
Salinity ( seawater)
mb
X
in Hg
Boiling Point 101.5C Freezing Point -0.5C
0
100
50
mm Hg (torr)
15Tw 15ºC
Saturation Vapor Pressure (mb)
Rate of Evaporation and Condensation (kg m-2 s-1)
-50
0
50
0
50
100
CLEAR
CLEAR
Time (s)
Temperature (C)
Evaporation
Condensation
WRT Liquid
WRT Ice
Equilibrium
Freezing Point
Temperature (C)
RUN
Pressure Units
Pressure
Atm
-50
50
0
1013.15
PAUSE
Salinity ( seawater)
mb
X
in Hg
Boiling Point 101.5C Freezing Point -0.5C
0
100
50
mm Hg (torr)
16Tw 15ºC
Saturation Vapor Pressure
Rate of Evaporation and Condensation (kg m-2 s-1)
-50
0
50
0
50
100
CLEAR
CLEAR
Time (s)
Temperature (C)
Evaporation
Condensation
WRT Liquid
WRT Ice
Equilibrium
Freezing Point
Temperature (C)
RUN
Pressure Units
Pressure
Atm
-50
50
0
1013.15
PAUSE
Salinity ( seawater)
mb
X
in Hg
Boiling Point 101.5C Freezing Point -0.5C
0
100
50
mm Hg (torr)
17Tw 15ºC
Saturation Vapor Pressure
Rate of Evaporation and Condensation (kg m-2 s-1)
-50
0
50
0
50
100
CLEAR
CLEAR
Time (s)
Temperature (C)
Evaporation
Condensation
WRT Liquid
WRT Ice
Equilibrium
Freezing Point
Temperature (C)
RUN
Pressure Units
Pressure
Atm
-50
50
0
1013.15
PAUSE
Salinity ( seawater)
mb
X
in Hg
Boiling Point 101.5C Freezing Point -0.5C
0
100
50
mm Hg (torr)
18Saturation Vapor Pressure as a Problem of
Equilibrium
- Assessment
- Java Applet Questions
- Example
- How does saturation vapor pressure change with
an increase in temperature? - Increases
- Decreases
- Remains the same
19Saturation Vapor Pressure as a Problem of
Equilibrium
20Group B
- Topics
- Saturation Vapor Pressure as a Problem of
Equilibrium - Solute and Curvature Effects as Applied to a
Kohler Curve
21Solute and Curvature Effects as Applied to a
Kohler Curve
- Learning Goals
- The student should be able to define
- Critical Radius
- Critical Supersaturation
- Haze Droplet
- Activation
- Cloud Condensation Nuclei
22Solute and Curvature Effects as Applied to a
Kohler Curve
- Learning Goals
- The student should be able to
- Describe the effect of CCN size on
- critical supersaturation
- critical radius
- Describe the effect of CCN type on
- critical supersaturation
- critical radius
23Solute and Curvature Effects as Applied to a
Kohler Curve
- Learning Goals
- The student should be able to
- Describe the effect of humidity on droplet size
24Solute and Curvature Effects as Applied to a
Kohler Curve
- Teaching Strategy
- Lecture
- Exploratory
25Solute and Curvature Effects as Applied to a
Kohler Curve
- Teaching Strategy
- Lecture
- Discussion of Learning Objective Content
- Power Point Lecture
- Exploratory
- Java Applet
- Active Learning
- In Class Exercise
- Homework
26Solute and Curvature Effects as Applied to a
Kohler Curve
- Java Applet
- Variables
- Temperature
- CCN Type
- CCN Size
- Super (or Sub) Saturation
- Droplet Radius
- Teaching Strategy
- Exploratory
27Solute and Curvature Effects as Applied to a
Kohler Curve
- Teaching Strategy
- Exploratory
- Java Applet
- Output
- Plot of Curvature Effect on es
- Plot of Solute Effect on es
- Combined Curvature and Solute Effects
- Animation of Droplet Growth/Evaporation
28Solute Effect
Curvature Effect
Combined Effects of Curvature and Solute Terms
Supersaturation
Supersaturation
1.0
0.01
0.1
100
1.0
10
0.01
0.1
100
1.0
10
Radius (mm)
Radius (mm)
CLEAR
PLOT
CLEAR
Kohler Curve Application Problem
Particle Type
Temperature
Pure H2O
X
(NH4)2SO4
15.0ºC
Initial Droplet Radius (mm)
NaCl
NH4NO3
H2SO4
Mineral Dust
RUN
NH4HSO4
Soot
Environmental Supersaturation
CCN Effective Radius (mm)
CCN Mass (kg)
1.2
0.8
1.0
10-17
0.01
0.1
1.0
10-19
10-18
10
29Solute Effect
Curvature Effect
Combined Effects of Curvature and Solute Terms
Supersaturation
Supersaturation
1.0
0.01
0.1
100
1.0
10
0.01
0.1
100
1.0
10
Radius (mm)
Radius (mm)
CLEAR
PLOT
CLEAR
Kohler Curve Application Problem
Particle Type
Temperature
Pure H2O
X
(NH4)2SO4
15.0ºC
Initial Droplet Radius (mm)
NaCl
NH4NO3
H2SO4
Mineral Dust
RUN
NH4HSO4
Soot
Environmental Supersaturation
CCN Effective Radius (mm)
CCN Mass (kg)
1.2
0.8
1.0
10-17
0.01
0.1
1.0
10-19
10-18
10
30Solute Effect
Curvature Effect
Combined Effects of Curvature and Solute Terms
Supersaturation
Supersaturation
1.0
0.01
0.1
100
1.0
10
0.01
0.1
100
1.0
10
Radius (mm)
Radius (mm)
CLEAR
PLOT
CLEAR
Kohler Curve Application Problem
Particle Type
Temperature
Pure H2O
(NH4)2SO4
15.0ºC
Initial Droplet Radius (mm)
NaCl
X
NH4NO3
H2SO4
Mineral Dust
RUN
NH4HSO4
Soot
Environmental Supersaturation
CCN Effective Radius (mm)
CCN Mass (kg)
1.2
0.8
1.0
10-17
0.01
0.1
1.0
10-19
10-18
10
31Solute Effect
Curvature Effect
Combined Effects of Curvature and Solute Terms
Supersaturation
Supersaturation
1.0
0.01
0.1
100
1.0
10
0.01
0.1
100
1.0
10
Radius (mm)
Radius (mm)
CLEAR
PLOT
CLEAR
Kohler Curve Application Problem
Particle Type
Temperature
Pure H2O
(NH4)2SO4
15.0ºC
Initial Droplet Radius (mm)
NaCl
X
NH4NO3
H2SO4
Mineral Dust
RUN
NH4HSO4
Soot
Environmental Supersaturation
CCN Effective Radius (mm)
CCN Mass (kg)
1.2
0.8
1.0
10-17
0.01
0.1
1.0
10-19
10-18
10
32Solute Effect
Curvature Effect
Combined Effects of Curvature and Solute Terms
Supersaturation
Supersaturation
1.0
0.01
0.1
100
1.0
10
0.01
0.1
100
1.0
10
Radius (mm)
Radius (mm)
CLEAR
PLOT
CLEAR
Kohler Curve Application Problem
Particle Type
Temperature
Pure H2O
(NH4)2SO4
15.0ºC
Initial Droplet Radius (mm)
NaCl
X
NH4NO3
H2SO4
Mineral Dust
RUN
0.01
0.1
100
1.0
10
NH4HSO4
Soot
Environmental Supersaturation
CCN Effective Radius (mm)
CCN Mass (kg)
1.2
0.8
1.0
10-17
0.01
0.1
1.0
10-19
10-18
10
33Solute Effect
Curvature Effect
Combined Effects of Curvature and Solute Terms
Supersaturation
Supersaturation
1.0
0.01
0.1
100
1.0
10
0.01
0.1
100
1.0
10
Radius (mm)
Radius (mm)
CLEAR
PLOT
CLEAR
Kohler Curve Application Problem
Particle Type
Temperature
Pure H2O
(NH4)2SO4
15.0ºC
Initial Droplet Radius (mm)
NaCl
X
NH4NO3
H2SO4
Mineral Dust
RUN
NH4HSO4
Soot
Environmental Supersaturation
CCN Effective Radius (mm)
CCN Mass (kg)
1.2
0.8
1.0
10-17
0.01
0.1
1.0
10-19
10-18
10
34Solute Effect
Curvature Effect
Combined Effects of Curvature and Solute Terms
Supersaturation
Supersaturation
1.0
0.01
0.1
100
1.0
10
0.01
0.1
100
1.0
10
Radius (mm)
Radius (mm)
CLEAR
PLOT
CLEAR
Kohler Curve Application Problem
Particle Type
Temperature
Pure H2O
(NH4)2SO4
15.0ºC
Initial Droplet Radius (mm)
NaCl
X
NH4NO3
H2SO4
Mineral Dust
RUN
NH4HSO4
Soot
Environmental Supersaturation
CCN Effective Radius (mm)
CCN Mass (kg)
1.2
0.8
1.0
10-17
0.01
0.1
1.0
10-19
10-18
10
35Solute Effect
Curvature Effect
Combined Effects of Curvature and Solute Terms
Supersaturation
Supersaturation
1.0
0.7 mm NaCl
0.01
0.1
100
1.0
10
0.01
0.1
100
1.0
10
Radius (mm)
Radius (mm)
CLEAR
PLOT
CLEAR
Kohler Curve Application Problem
Particle Type
Temperature
Pure H2O
(NH4)2SO4
15.0ºC
Initial Droplet Radius (mm)
NaCl
X
NH4NO3
H2SO4
Mineral Dust
RUN
NH4HSO4
Soot
Environmental Supersaturation
CCN Effective Radius (mm)
CCN Mass (kg)
1.2
0.8
1.0
10-17
0.01
0.1
1.0
10-19
10-18
10
36Solute Effect
Curvature Effect
Combined Effects of Curvature and Solute Terms
Supersaturation
Supersaturation
1.0
0.01
0.1
100
1.0
10
0.01
0.1
100
1.0
10
Radius (mm)
Radius (mm)
CLEAR
PLOT
CLEAR
Kohler Curve Application Problem
Particle Type
Temperature
Pure H2O
(NH4)2SO4
15.0ºC
Initial Droplet Radius (mm)
NaCl
X
NH4NO3
H2SO4
Mineral Dust
RUN
NH4HSO4
Soot
Environmental Supersaturation
CCN Effective Radius (mm)
CCN Mass (kg)
1.2
0.8
1.0
10-17
0.01
0.1
1.0
10-19
10-18
10
37Solute Effect
Curvature Effect
Combined Effects of Curvature and Solute Terms
Supersaturation
Supersaturation
1.0
0.3 mm H2SO4
0.01
0.1
100
1.0
10
0.01
0.1
100
1.0
10
Radius (mm)
Radius (mm)
CLEAR
PLOT
CLEAR
Kohler Curve Application Problem
Particle Type
Temperature
Pure H2O
(NH4)2SO4
15.0ºC
Initial Droplet Radius (mm)
NaCl
NH4NO3
H2SO4
X
Mineral Dust
RUN
NH4HSO4
Soot
Environmental Supersaturation
CCN Effective Radius (mm)
CCN Mass (kg)
1.2
0.8
1.0
10-17
0.01
0.1
1.0
10-19
10-18
10
38Solute Effect
Curvature Effect
Combined Effects of Curvature and Solute Terms
Supersaturation
Supersaturation
1.0
0.3 mm NaCl
0.3 mm H2SO4
0.01
0.1
100
1.0
10
0.01
0.1
100
1.0
10
Radius (mm)
Radius (mm)
CLEAR
PLOT
CLEAR
Kohler Curve Application Problem
Particle Type
Temperature
Pure H2O
(NH4)2SO4
15.0ºC
Initial Droplet Radius (mm)
NaCl
X
NH4NO3
H2SO4
Mineral Dust
RUN
NH4HSO4
Soot
Environmental Supersaturation
CCN Effective Radius (mm)
CCN Mass (kg)
1.2
0.8
1.0
10-17
0.01
0.1
1.0
10-19
10-18
10
39Solute Effect
Curvature Effect
Combined Effects of Curvature and Solute Terms
Supersaturation
Supersaturation
1.0
0.3 mm NaCl
0.3 mm H2SO4
0.01
0.1
100
1.0
10
0.01
0.1
100
1.0
10
Radius (mm)
Radius (mm)
CLEAR
PLOT
CLEAR
Kohler Curve Application Problem
Particle Type
Temperature
Pure H2O
(NH4)2SO4
15.0ºC
Initial Droplet Radius (mm)
NaCl
X
NH4NO3
H2SO4
Mineral Dust
RUN
NH4HSO4
Soot
Environmental Supersaturation
CCN Effective Radius (mm)
CCN Mass (kg)
1.2
0.8
1.0
10-17
0.01
0.1
1.0
10-19
10-18
10
40Solute Effect
Curvature Effect
Combined Effects of Curvature and Solute Terms
Supersaturation
Supersaturation
1.0
0.3 mm NaCl
0.3 mm H2SO4
0.01
0.1
100
1.0
10
0.01
0.1
100
1.0
10
Radius (mm)
Radius (mm)
CLEAR
PLOT
CLEAR
Kohler Curve Application Problem
Particle Type
Temperature
Pure H2O
(NH4)2SO4
15.0ºC
Initial Droplet Radius (mm)
NaCl
X
NH4NO3
H2SO4
Mineral Dust
RUN
NH4HSO4
Soot
Environmental Supersaturation
CCN Effective Radius (mm)
CCN Mass (kg)
1.2
0.8
1.0
10-17
0.01
0.1
1.0
10-19
10-18
10
41Solute Effect
Curvature Effect
Combined Effects of Curvature and Solute Terms
Supersaturation
Supersaturation
1.0
0.3 mm NaCl
0.3 mm H2SO4
0.01
0.1
100
1.0
10
0.01
0.1
100
1.0
10
Radius (mm)
Radius (mm)
CLEAR
PLOT
CLEAR
Kohler Curve Application Problem
Particle Type
Temperature
Pure H2O
(NH4)2SO4
15.0ºC
Initial Droplet Radius (mm)
NaCl
X
NH4NO3
H2SO4
Mineral Dust
RUN
NH4HSO4
Soot
Environmental Supersaturation
CCN Effective Radius (mm)
CCN Mass (kg)
1.2
0.8
1.0
10-17
0.01
0.1
1.0
10-19
10-18
10
42Solute Effect
Curvature Effect
Combined Effects of Curvature and Solute Terms
Supersaturation
Supersaturation
1.0
0.3 mm NaCl
0.3 mm H2SO4
0.01
0.1
100
1.0
10
0.01
0.1
100
1.0
10
Radius (mm)
Radius (mm)
CLEAR
PLOT
CLEAR
Kohler Curve Application Problem
Particle Type
Temperature
Pure H2O
(NH4)2SO4
15.0ºC
Initial Droplet Radius (mm)
NaCl
X
NH4NO3
H2SO4
Mineral Dust
RUN
0.01
0.1
100
1.0
10
NH4HSO4
Soot
Environmental Supersaturation
CCN Effective Radius (mm)
CCN Mass (kg)
1.2
0.8
1.0
10-17
0.01
0.1
1.0
10-19
10-18
10
43Solute Effect
Curvature Effect
Combined Effects of Curvature and Solute Terms
Supersaturation
Supersaturation
1.0
0.3 mm NaCl
0.3 mm H2SO4
0.01
0.1
100
1.0
10
0.01
0.1
100
1.0
10
Radius (mm)
Radius (mm)
CLEAR
PLOT
CLEAR
Kohler Curve Application Problem
Particle Type
Temperature
Pure H2O
(NH4)2SO4
15.0ºC
Initial Droplet Radius (mm)
NaCl
X
NH4NO3
H2SO4
Mineral Dust
RUN
0.01
0.1
100
1.0
10
NH4HSO4
Soot
Environmental Supersaturation
CCN Effective Radius (mm)
CCN Mass (kg)
1.2
0.8
1.0
10-17
0.01
0.1
1.0
10-19
10-18
10
44Solute Effect
Curvature Effect
Combined Effects of Curvature and Solute Terms
Supersaturation
Supersaturation
1.0
0.3 mm NaCl
0.3 mm H2SO4
0.01
0.1
100
1.0
10
0.01
0.1
100
1.0
10
Radius (mm)
Radius (mm)
CLEAR
PLOT
CLEAR
Kohler Curve Application Problem
Particle Type
Temperature
Pure H2O
(NH4)2SO4
15.0ºC
Initial Droplet Radius (mm)
NaCl
X
NH4NO3
H2SO4
Mineral Dust
RUN
0.01
0.1
100
1.0
10
NH4HSO4
Soot
Environmental Supersaturation
CCN Effective Radius (mm)
CCN Mass (kg)
1.2
0.8
1.0
10-17
0.01
0.1
1.0
10-19
10-18
10
45Solute Effect
Curvature Effect
Combined Effects of Curvature and Solute Terms
Supersaturation
Supersaturation
1.0
0.3 mm NaCl
0.3 mm H2SO4
0.01
0.1
100
1.0
10
0.01
0.1
100
1.0
10
Radius (mm)
Radius (mm)
CLEAR
PLOT
CLEAR
Kohler Curve Application Problem
Particle Type
Temperature
Pure H2O
(NH4)2SO4
15.0ºC
Initial Droplet Radius (mm)
NaCl
X
NH4NO3
H2SO4
Mineral Dust
RUN
0.01
0.1
100
1.0
10
NH4HSO4
Soot
Environmental Supersaturation
CCN Effective Radius (mm)
CCN Mass (kg)
1.2
0.8
1.0
10-17
0.01
0.1
1.0
10-19
10-18
10
46Solute Effect
Curvature Effect
Combined Effects of Curvature and Solute Terms
Supersaturation
Supersaturation
1.0
0.3 mm NaCl
0.3 mm H2SO4
0.01
0.1
100
1.0
10
0.01
0.1
100
1.0
10
Radius (mm)
Radius (mm)
CLEAR
PLOT
CLEAR
Kohler Curve Application Problem
Particle Type
Temperature
Pure H2O
(NH4)2SO4
15.0ºC
Initial Droplet Radius (mm)
NaCl
X
NH4NO3
H2SO4
Mineral Dust
RUN
0.01
0.1
100
1.0
10
NH4HSO4
Soot
Environmental Supersaturation
CCN Effective Radius (mm)
CCN Mass (kg)
1.2
0.8
1.0
10-17
0.01
0.1
1.0
10-19
10-18
10
47Solute Effect
Curvature Effect
Combined Effects of Curvature and Solute Terms
Supersaturation
Supersaturation
1.0
0.3 mm NaCl
0.3 mm H2SO4
0.01
0.1
100
1.0
10
0.01
0.1
100
1.0
10
Radius (mm)
Radius (mm)
CLEAR
PLOT
CLEAR
Kohler Curve Application Problem
Particle Type
Temperature
Pure H2O
(NH4)2SO4
15.0ºC
Initial Droplet Radius (mm)
NaCl
X
NH4NO3
H2SO4
Mineral Dust
RUN
0.01
0.1
100
1.0
10
NH4HSO4
Soot
Environmental Supersaturation
CCN Effective Radius (mm)
CCN Mass (kg)
1.2
0.8
1.0
10-17
0.01
0.1
1.0
10-19
10-18
10
48Solute Effect
Curvature Effect
Combined Effects of Curvature and Solute Terms
Supersaturation
Supersaturation
1.0
0.3 mm NaCl
0.3 mm H2SO4
0.01
0.1
100
1.0
10
0.01
0.1
100
1.0
10
Radius (mm)
Radius (mm)
CLEAR
PLOT
CLEAR
Kohler Curve Application Problem
Particle Type
Temperature
Pure H2O
(NH4)2SO4
15.0ºC
Initial Droplet Radius (mm)
NaCl
X
NH4NO3
H2SO4
Mineral Dust
RUN
0.01
0.1
100
1.0
10
NH4HSO4
Soot
Environmental Supersaturation
CCN Effective Radius (mm)
CCN Mass (kg)
1.2
0.8
1.0
10-17
0.01
0.1
1.0
10-19
10-18
10
49Solute Effect
Curvature Effect
Combined Effects of Curvature and Solute Terms
Supersaturation
Supersaturation
1.0
0.3 mm NaCl
0.3 mm H2SO4
0.01
0.1
100
1.0
10
0.01
0.1
100
1.0
10
Radius (mm)
Radius (mm)
CLEAR
PLOT
CLEAR
Kohler Curve Application Problem
Particle Type
Temperature
Pure H2O
(NH4)2SO4
15.0ºC
Initial Droplet Radius (mm)
NaCl
X
NH4NO3
H2SO4
Mineral Dust
RUN
0.01
0.1
100
1.0
10
NH4HSO4
Soot
Environmental Supersaturation
CCN Effective Radius (mm)
CCN Mass (kg)
1.2
0.8
1.0
10-17
0.01
0.1
1.0
10-19
10-18
10
50Solute Effect
Curvature Effect
Combined Effects of Curvature and Solute Terms
Supersaturation
Supersaturation
1.0
0.3 mm NaCl
0.3 mm H2SO4
0.01
0.1
100
1.0
10
0.01
0.1
100
1.0
10
Radius (mm)
Radius (mm)
CLEAR
PLOT
CLEAR
Kohler Curve Application Problem
Particle Type
Temperature
Pure H2O
(NH4)2SO4
15.0ºC
Initial Droplet Radius (mm)
NaCl
X
NH4NO3
H2SO4
Mineral Dust
RUN
0.01
0.1
100
1.0
10
NH4HSO4
Soot
Environmental Supersaturation
CCN Effective Radius (mm)
CCN Mass (kg)
1.2
0.8
1.0
10-17
0.01
0.1
1.0
10-19
10-18
10
51Solute Effect
Curvature Effect
Combined Effects of Curvature and Solute Terms
Supersaturation
Supersaturation
1.0
0.3 mm NaCl
0.3 mm H2SO4
0.01
0.1
100
1.0
10
0.01
0.1
100
1.0
10
Radius (mm)
Radius (mm)
CLEAR
PLOT
CLEAR
Kohler Curve Application Problem
Particle Type
Temperature
Pure H2O
(NH4)2SO4
15.0ºC
Initial Droplet Radius (mm)
NaCl
X
NH4NO3
H2SO4
Mineral Dust
RUN
0.01
0.1
100
1.0
10
NH4HSO4
Soot
Environmental Supersaturation
CCN Effective Radius (mm)
CCN Mass (kg)
1.2
0.8
1.0
10-17
0.01
0.1
1.0
10-19
10-18
10
52Solute Effect
Curvature Effect
Combined Effects of Curvature and Solute Terms
Supersaturation
Supersaturation
1.0
0.3 mm NaCl
0.3 mm H2SO4
0.01
0.1
100
1.0
10
0.01
0.1
100
1.0
10
Radius (mm)
Radius (mm)
CLEAR
PLOT
CLEAR
Kohler Curve Application Problem
Particle Type
Temperature
Pure H2O
(NH4)2SO4
15.0ºC
Initial Droplet Radius (mm)
NaCl
X
NH4NO3
H2SO4
Mineral Dust
RUN
0.01
0.1
100
1.0
10
NH4HSO4
Soot
Environmental Supersaturation
CCN Effective Radius (mm)
CCN Mass (kg)
1.2
0.8
1.0
10-17
0.01
0.1
1.0
10-19
10-18
10
53Saturation Vapor Pressure as a Problem of
Equilibrium
- Assessment
- Java Applet Questions
- Example
- The addition of a solute to a pure water droplet
will cause the es to ________. - Increase
- Decrease
- Remains the same