- •5. Physical Properties
- •5.1 Solubilities
- •Table 5.1 Solubility of Gases in Water
- •5.2 Vapor Pressures
- •Table 5.8 Vapor Pressures of Various Inorganic Compounds
- •5.3 Boiling Points
- •Table 5.12 Ternary Azeotropic Mixtures
- •5.4 Freezing Mixtures
- •5.5 Density and Specific Gravity
- •Table 5.14 Density of Mercury and Water
- •5.5.1 Density of Moist Air
- •Table 5.17 Dielectric Constant (Permittivity) and Dipole Moment of Various Organic Substances
- •5.6.1 Refractive Index
- •5.6.2 Surface Tension
- •5.6.3 Dipole Moments
- •5.6.4 Dielectric Constants
- •5.6.5 Viscosity
- •Table 5.22 Aqueous Sucrose Solutions
- •5.7 Combustible Mixtures
- •Table 5.23 Properties of Combustible Mixtures in Air
- •5.8 Thermal Conductivity
- •Table 5.26 Thermal Conductivity of Various Solids
- •5.9 Miscellany
- •Table 5.29 Van der Waals’ Constants for Gases
- •5.9.1 Some Physical Chemistry Equations for Gases
PHYSICAL PROPERTIES |
5.137 |
where the summation extends over all charges (electrons and nuclei) in the molecule. The numerical
values of the dipole moment, expressed in the c.g.s. system of units, are in debye units, D, where
1 D 10 18 esu of charge |
centimeters. |
The conversion factor to SI units is |
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1 D 3.335 64 |
10 30 |
C · m |
[coulomb-meter] |
Tables 5.17 and 5.18 contain a selected group of compounds for which the dipole moment is |
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given. An extensive |
collection |
of |
dipole moments (approximately 7000 |
entries) |
is contained in |
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A. L. McClellan, |
Tables |
of Experimental Dipole Moments, |
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W. H. Freeman, San Francisco, 1963. A |
critical survey of 500 compounds in the gas phase is given by Nelson, Lide, and Maryott, NSRDSNBS 10, Washington, D.C., 1967.
5.6.4 Dielectric Constants
If two oppositely charged plates exist in a vacuum, there is a certain force of attraction between them, as stated by Coulomb’s law:
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q1 q2 |
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F |
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· r 2 |
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4 0 |
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where |
F is the force, in newtons, acting on each of the charges |
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q1 |
and q2 ,r is the distance between |
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the charges, is the dielectric constant of the medium between the plates, and |
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0 |
is the permittivity |
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of free |
space. |
q1 ,q2 |
are expressed in coulombs |
and |
r in meters. If |
another substance, |
such as a |
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solvent, is in the space separating these charges (or ions in a solution), their attraction for each other |
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is less. The dielectric constant is a measure of the relative effect a solvent has on the force with |
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which two oppositely charged plates attract each other. The dielectric constant is a unitless number. |
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Dielectric constants for a selected group of inorganic and organic compounds are included in |
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Tables 5.17 and 5.18. An extensive list has been compiled by Maryott and Smith, |
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National Bureau |
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Standards |
Circular 514, |
Washington, D.C., 1951. |
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For gases the values of the dielectric constant can be adjusted to somewhat different conditions |
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of temperature and pressure by means of the equation |
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( 1)t,p |
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p |
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( 1)20 ,1 atm |
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760[1 0.003 411( |
t 20)] |
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where |
p is the pressure (in mmHg) and |
t is the temperature (in |
C). The errors associated with this |
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equation probably do not exceed 0.02% for gases between 10 and 30 |
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C and for pressures between |
700 and 800 mm. The dielectric constants of selected gases will be found in Table. 5.18.
5.6.5Viscosity
The |
dynamic viscosity, |
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or coefficient of viscosity, |
of a Newtonian fluid is defined as the force per |
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unit area necessary to maintain a unit velocity gradient at right angles to the direction of flow between |
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two parallel planes |
a unit distance apart. The SI unit is pascal-second or newton-second per meter |
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squared |
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2 |
The].c.g.s. unit of viscosity is the poise [P]; |
1 cP |
2 |
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[N · s · m |
1 mN ·Thesdynamic· . |
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viscosity |
decreases |
with |
the |
temperature approximately according |
to the |
equation: log |
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A B /T . Values of |
A |
and B for a large number of liquids are given by Barrer, |
Trans. Faraday Soc. |
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39: |
48 (1943). |
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5.138 |
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SECTION |
5 |
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TABLE 5.21 |
Aqueous Glycerol Solutions |
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Relative |
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Viscosity, mN · s · m |
2 |
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% Weight |
Grams |
density |
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glycerol |
per liter |
25 /25C |
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20 C |
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25 C |
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30 C |
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100 |
1261 |
1.262 01 |
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1 495 |
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942 |
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622 |
99 |
1246 |
1.259 45 |
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1 194 |
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772 |
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509 |
98 |
1231 |
1.256 85 |
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971 |
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627 |
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423 |
97 |
1216 |
1.254 25 |
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802 |
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521 |
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353 |
96 |
1201 |
1.251 65 |
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659 |
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434 |
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296 |
95 |
1186 |
1.249 10 |
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543.5 |
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365 |
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248 |
80 |
966.8 |
1.209 25 |
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61.8 |
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45.72 |
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34.81 |
50 |
563.2 |
1.127 20 |
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6.032 |
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5.024 |
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4.233 |
25 |
265.0 |
1.061 15 |
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2.089 |
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1.805 |
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1.586 |
10 |
102.2 |
1.023 70 |
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1.307 |
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1.149 |
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1.021 |
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Kinematic viscosity v |
is the ratio |
of the |
dynamic |
viscosity to |
the density of a fluid. The |
SI |
unit |
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is meter squared per second |
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1 |
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are called stokes |
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[cm |
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1]; poises |
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[mThe·c.sg.]s. units |
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· s |
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stokes |
density. |
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Fluidity |
is the reciprocal of the dynamic viscosity. |
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The primary reference liquid for viscosity measurements is water. The absolute viscosity of water |
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at 20 C |
is |
1.0019 ( |
0.0003) |
mN · s · m |
2 |
(or centipoise), as determined by Swindells, Coe, and |
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Godfrey, J. Research Natl. Bur. Standards |
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48: |
1 (1952). The relative viscosity of water, |
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is / 20 , |
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0.8885 at 25 C, 0.7960 at 30 |
C, and 0.6518 at 40 |
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C. Values at temperatures between 15 and 60 |
C |
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are best represented by Cragoe’s equation: |
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log |
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1.2348(20 |
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t) 0.001 467( |
t 20) |
2 |
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20 |
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t |
96 |
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The |
Reynolds number |
for flow in a tube is defined by |
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/ , |
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d |
is the diameter of the tube, |
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wheredv |
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is the density of the fluid, and |
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is its dynamic |
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vis the average velocity of the fluid along the tube, |
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viscosity. At flow velocities corresponding with values of the Reynolds number of greater than 2000, |
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turbulence is encountered. |
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TABLE 5.22 Aqueous Sucrose Solutions |
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Relative |
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Viscosity, mN · s · m |
2 |
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% Weight |
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Grams |
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density |
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15 C |
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20 |
C |
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25 C |
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sucrose |
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per liter |
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20 /4 C |
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75 |
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1034 |
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1.379 0 |
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4 039 |
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2 328 |
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1 405 |
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70 |
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943.0 |
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1.347 2 |
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746.9 |
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481.6 |
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321.6 |
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65 |
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855.6 |
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1.316 3 |
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211.3 |
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147.2 |
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105.4 |
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60 |
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771.9 |
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1.286 5 |
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79.49 |
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58.49 |
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40.03 |
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50 |
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614.8 |
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1.299 6 |
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19.53 |
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15.43 |
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12.40 |
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40 |
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470.6 |
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1.176 4 |
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7.463 |
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6.167 |
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5.164 |
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30 |
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338.1 |
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1.127 0 |
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3.757 |
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3.187 |
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2.735 |
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