- •Preface
- •Calculus
- •Introduction to calculus
- •The concept of differentiation
- •The concept of integration
- •How derivatives and integrals relate to one another
- •Symbolic versus numerical calculus
- •Numerical differentiation
- •Numerical integration
- •Physics
- •Metric prefixes
- •Areas and volumes
- •Common geometric shapes
- •Unit conversions and physical constants
- •Unity fractions
- •Conversion formulae for temperature
- •Conversion factors for distance
- •Conversion factors for volume
- •Conversion factors for velocity
- •Conversion factors for mass
- •Conversion factors for force
- •Conversion factors for area
- •Conversion factors for pressure (either all gauge or all absolute)
- •Conversion factors for pressure (absolute pressure units only)
- •Conversion factors for energy or work
- •Conversion factors for power
- •Terrestrial constants
- •Properties of water
- •Miscellaneous physical constants
- •Weight densities of common materials
- •Dimensional analysis
- •The International System of Units
- •Conservation Laws
- •Classical mechanics
- •Work, energy, and power
- •Mechanical springs
- •Rotational motion
- •Simple machines
- •Levers
- •Pulleys
- •Inclined planes
- •Gears
- •Belt drives
- •Chain drives
- •Elementary thermodynamics
- •Heat versus Temperature
- •Temperature
- •Heat
- •Heat transfer
- •Phase changes
- •Phase diagrams and critical points
- •Saturated steam table
- •Thermodynamic degrees of freedom
- •Applications of phase changes
- •Fluid mechanics
- •Pressure
152 |
CHAPTER 2. PHYSICS |
2.10.7Phase diagrams and critical points
A comprehensive way of describing the relationship between pressure, temperature, and substance phase is with something called a phase diagram. With pressure shown on one axis, and temperature on the other, a phase diagram describes the various phases of a substance in possible equilibrium at certain pressure/temperature combinations.
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Phase diagram for water |
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Pcritical |
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218 atm |
|
Critical point |
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Freezing |
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Melting |
Liquid |
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Pressure |
Solid |
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(P) |
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Condensing |
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Boiling |
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Ptriple |
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Vapor |
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0.006 atm |
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|
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Sublimation |
Triple point |
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|
Sublimation |
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Temperature |
|
|
Ttriple |
(T) |
Tcritical |
|
0.01 deg C |
|
374 deg C |
This phase diagram (for water) illustrates some of the features common to all phase diagrams: curved lines define the boundaries between solid, liquid, and vapor phases; the point of intersection of these three curves is where the substance may exist in all three phases simultaneously (called the triple point48) and points where a curve simply ends within the span of the graph indicate critical points, where the certain phases cease to exist.
The curved line from the triple point up and to the right defines the boundary between liquid water and water vapor. Each point on that line represents a set of unique pressure and temperature conditions for boiling (changing phase from liquid to vapor) or for condensation (changing phase from vapor to liquid). As you can see, increased pressure results in an increased boiling point (i.e. at higher pressures, water must be heated to greater temperatures before boiling may take place).
48When H2O is at its triple point, vapor (steam), liquid (water), and solid (ice) of water will co-exist in the same space. One way to visualize the triple point is to consider it the pressure at which the boiling and freezing temperatures of a substance become the same.
2.10. ELEMENTARY THERMODYNAMICS |
153 |
In fact, the whole concept of a singular boiling point for water becomes quaint in the light of a phase diagram: boiling is seen to occur over a wide range of temperatures49, the exact temperature varying with pressure.
Something interesting happens when the temperature is raised above a certain value called the critical temperature. At this value (approximately 374 degrees Celsius for water), no amount of pressure will maintain it in a liquid state. Water, once heated beyond 374 degrees Celsius, is no longer a liquid and may only exist in a stable condition as a vapor. The critical pressure of any substance is the pressure value at the liquid/vapor boundary at the point of critical temperature.
A vivid example of critical temperature is this photograph of an ultra-high pressure storage vessel for oxygen gas, at a rocket engine testing facility:
The critical temperature for oxygen is 154.58 Kelvin, which is equal to −118.57 degrees Celsius or −181.43 degrees Fahrenheit. Since this pressure vessel is completely uninsulated, we know the temperature of the oxygen inside of it will be the same (or nearly the same) as ambient temperature, which is obviously much warmer than −118.57 oC. Since the oxygen’s temperature is well above the critical temperature for the element oxygen, we may safely conclude that the oxygen inside this vessel must exist as a gas. Even at the extremely high pressure this vessel is capable of holding (15000 PSIG), the oxygen cannot liquefy.
The slightly curved line from the triple point up and to the left defines the boundary between solid ice and liquid water. As you can see, the near-vertical pitch of this curve suggests the freezing temperature of water is quite stable over a wide pressure range.
49Anywhere between the triple-point temperature and the critical temperature, to be exact.
154 |
CHAPTER 2. PHYSICS |
Carbon dioxide exhibits a di erent set of curves than water on its phase diagram, with its own unique critical temperature and pressure values:
Pcritical
72.9 atm
Pressure
(P)
Ptriple
5.11 atm
Phase diagram for carbon dioxide
Freezing |
Critical point |
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Melting |
Liquid |
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Solid |
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Condensing |
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Boiling |
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Vapor |
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Sublimation |
Triple point |
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Sublimation |
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Temperature |
|
Ttriple |
(T) |
Tcritical |
-56.6 deg C |
|
31 deg C |
Note how the triple-point pressure of carbon dioxide is well above ambient conditions on Earth. This means carbon dioxide is not stable in its liquid state unless put under substantial pressure (at least 60.4 PSIG). This is why solid carbon dioxide is referred to as dry ice: it does not liquefy with the application of heat, rather it sublimates directly into its vapor phase.
Another interesting di erence between the carbon dioxide and water phase diagrams is the slope of the solid/liquid boundary line. With water, this boundary drifts to the left (lower temperature) as pressure increases. With carbon dioxide, this boundary drifts to the right (higher temperature) as pressure increases. Whether the fusion temperature increases or decreases with increasing pressure marks whether that substance contracts or expands as it transitions from liquid to solid. Carbon dioxide, like most pure substances, contracts to a smaller volume when it goes from liquid to solid, and its fusion curve drifts to the right as pressure increases. Water is unusual in this regard, expanding to a larger volume when freezing, and its fusion curve drifts to the left as pressure increases.
2.10. ELEMENTARY THERMODYNAMICS |
155 |
2.10.8Saturated steam table
A saturated steam table shows temperatures and pressures for water at the liquid/vapor transition (i.e. points lying along the liquid/vapor interface shown in a phase change diagram), as well as enthalpy values for the water and steam under those conditions. The sensible heat of water is the amount of thermal energy per pound necessary to raise water’s temperature from the freezing point to the boiling point. The latent heat of vapor is the amount of energy per pound necessary to convert water (liquid) into steam (vapor). The total heat is the enthalpy of steam (thermal energy per pound) between the listed condition in the table and the freezing temperature of water.
By definition a saturated steam table does not describe steam at temperatures greater than the boiling point. For such purposes, a superheated steam table is necessary.
156 |
CHAPTER 2. PHYSICS |
Data for this saturated steam table was taken from Thermal Properties of Saturated and Superheated Steam by Lionel Marks and Harvey Davis, published in 1920 by Longmans, Green, and Company.
Saturated Steam Table
Temperature |
Pressure |
Sensible heat of |
Latent heat of |
Total heat |
(Deg F) |
(PSIA) |
liquid (BTU/lb) |
vapor (BTU/lb) |
(BTU/lb) |
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|
|
|
|
32 |
0.0886 |
0.00 |
1073.4 |
1073.4 |
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|
|
|
|
40 |
0.1217 |
8.05 |
1068.9 |
1076.9 |
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50 |
0.1780 |
18.08 |
1063.3 |
1081.4 |
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60 |
0.2562 |
28.08 |
1057.8 |
1085.9 |
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70 |
0.3626 |
38.06 |
1052.3 |
1090.3 |
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|
80 |
0.505 |
48.03 |
1046.7 |
1094.8 |
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50 |
0.696 |
58.00 |
1041.2 |
1099.2 |
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60 |
0.2562 |
28.08 |
1057.8 |
1085.9 |
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70 |
0.3626 |
38.06 |
1052.3 |
1090.3 |
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|
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|
|
80 |
0.505 |
48.03 |
1046.7 |
1094.8 |
|
|
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|
|
90 |
0.696 |
58.00 |
1041.2 |
1099.2 |
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|
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|
100 |
0.946 |
67.97 |
1035.6 |
1103.6 |
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|
110 |
1.271 |
77.94 |
1030.0 |
1108.0 |
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|
120 |
1.689 |
87.91 |
1024.4 |
1112.3 |
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|
130 |
2.219 |
97.89 |
1018.8 |
1116.7 |
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|
140 |
2.885 |
107.87 |
1013.1 |
1121.0 |
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|
150 |
3.714 |
117.86 |
1007.4 |
1125.3 |
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|
160 |
4.737 |
127.86 |
1001.6 |
1129.5 |
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|
170 |
5.992 |
137.87 |
995.8 |
1133.7 |
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|
180 |
7.51 |
147.88 |
989.9 |
1137.8 |
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|
190 |
9.34 |
157.91 |
983.9 |
1141.8 |
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|
200 |
11.52 |
167.94 |
977.8 |
1145.8 |
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|
210 |
14.13 |
177.99 |
971.6 |
1149.6 |
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212 |
14.70 |
180.00 |
970.4 |
1150.4 |
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2.10. ELEMENTARY THERMODYNAMICS |
157 |
Saturated Steam Table (continued)
Temperature |
Pressure |
Sensible heat of |
Latent heat of |
Total heat |
(Deg F) |
(PSIA) |
liquid (BTU/lb) |
vapor (BTU/lb) |
(BTU/lb) |
|
|
|
|
|
220 |
17.19 |
188.1 |
965.2 |
1153.3 |
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|
230 |
20.77 |
198.2 |
958.7 |
1156.9 |
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240 |
24.97 |
208.3 |
952.1 |
1160.4 |
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250 |
29.82 |
218.5 |
945.3 |
1163.8 |
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|
260 |
35.42 |
228.6 |
938.4 |
1167.0 |
|
|
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|
270 |
41.85 |
238.8 |
931.4 |
1170.2 |
|
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|
|
280 |
49.18 |
249.0 |
924.3 |
1173.3 |
|
|
|
|
|
290 |
57.55 |
259.3 |
916.9 |
1176.2 |
|
|
|
|
|
300 |
67.00 |
269.6 |
909.5 |
1179.1 |
|
|
|
|
|
310 |
77.67 |
279.9 |
901.9 |
1181.8 |
|
|
|
|
|
320 |
89.63 |
290.2 |
894.2 |
1184.4 |
|
|
|
|
|
330 |
103.0 |
300.6 |
886.3 |
1186.9 |
|
|
|
|
|
340 |
118.0 |
311.0 |
878.3 |
1189.3 |
|
|
|
|
|
350 |
134.6 |
321.4 |
870.1 |
1191.5 |
|
|
|
|
|
360 |
153.0 |
331.9 |
861.8 |
1193.7 |
|
|
|
|
|
370 |
173.3 |
342.4 |
853.4 |
1195.8 |
|
|
|
|
|
380 |
195.6 |
352.9 |
844.8 |
1197.7 |
|
|
|
|
|
390 |
220.2 |
363.5 |
836.1 |
1199.6 |
|
|
|
|
|
400 |
247.1 |
374.1 |
827.2 |
1201.3 |
|
|
|
|
|
410 |
276.4 |
384.7 |
818.2 |
1202.9 |
|
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|
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|
420 |
308.4 |
395.4 |
809.0 |
1204.4 |
|
|
|
|
|
430 |
343.2 |
406.2 |
799.6 |
1205.8 |
|
|
|
|
|
440 |
380.8 |
417.0 |
790.1 |
1207.1 |
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