Appendix A: Viscosities and Other Properties of Gases and Liquids

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FIGURE A.1 Viscosities of various fluids at 1 atm pressure. 1 cP = 0.01 g/(cm s) = 6.72 × 10−4 lbm/(ft s) = 2.42 lbm/(ft h) = 2.09 × 10−5 lbf s/ft2. (Reproduced from Brown, G.G. et al., Unit Operations, Wiley, New York, 1951, p. 586. With permission.)

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FIGURE A.2 Viscosity of various liquids: (1) Carbon dioxide, (2) ammonia, (3) methyl chloride, (4) sulfur dioxide, (5) Freon 12, (6) Freon 114, (7) Freon 11, (8) Freon 113, (9) ethyl alcohol, (10) isopropyl alcohol, (11) 20% sulfuric acid—20% H2SO4, (12) Dowtherm E, (13) Dowtherm A, (14) 20% sodium hydroxide—20% NaOH, (15) mercury, (16) 10% sodium chloride brine—10% NaCl, (17) 20% sodium chloride brine—20% NaCl, (18) 10% calcium chloride brine—10% CaCl2, and (19) 20% calcium chloride brine—20% CaCl2. (From Crane Technical Paper 4–10, Crane Co., Chicago, IL, 1991.)

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FIGURE A.3 Viscosity of water and liquid petroleum products: (1) Ethane (C2H6), (2) propane (C3H8), (3) butane (C4H10), (4) natural gasoline, (5) gasoline, (6) water, (7) kerosene, (8) distillate, (9) 48° API crude, (10) 40° API crude, (11) 35.6° API crude, (12) 32.6° API crude, (13) salt creek crude, (14) Fuel 3 (Max.), (15) Fuel 5 (Min.), (16) SAE 10 lube (100 V.I.), (17) SAE 30 lube (100 V.I.), (18) Fuel 5 (Min.) or Fuel 6 (Min.), (19) SAE 70 lube (100 V.I.), (20) Bunker C fuel (Max.) and M.C. Residuum, and (21) asphalt. (From Crane Company, Crane Technical Paper 410, Crane Co., Chicago, IL, 1991.)

TABLE A.1
Viscosities of Liquids (Coordinates Apply to Figure A.4)

Liquid

X

Y

Acetaldehyde

15.2

4.8

Acetic acid, 100%

12.1

14.2

Acetic acid, 70%

9.5

17.0

Acetic anhydride

12.7

12.8

Acetone, 100%

14.5

7.2

Acetone, 35%

7.9

15.0

Acetonitrile

14.4

7.4

Acrylic acid

12.3

13.9

Allyl alcohol

10.2

14.3

Allyl bromide

14.4

9.6

Allyl iodide

14.0

11.7

Ammonia, 100%

12.6

2.0

Ammonia, 26%

10.1

13.9

Amyl acetate

11.8

12.5

Amyl alcohol

7.5

18.4

Aniline

8.1

18.7

Anisole

12.3

13.5

Arsenic trichloride

13.9

14.5

Benzene

12.5

10.9

Brine, CaCl(S)_2(S), 25%

6.6

15.9

Brine, NaCl, 25%

10.2

16.6

Bromine

14.2

13.2

Bromotoluene

20.0

15.9

Butyl acetate

12.3

11.0

Butyl acrylate

11.5

12.6

Butyl alcohol

8.6

17.2

Butyric acid

12.1

15.3

Carbon dioxide

11.6

0.3

Carbon disulfide

16.1

7.5

Carbon tetrachloride

12.7

13.1

Chlorobenzene

12.3

12.4

Chloroform

14.4

10.2

Chlorosulfonic acid

11.2

18.1

Chlorotoluene, ortho

13.0

13.3

Chlorotoluene, meta

13.3

12.5

Chlorotoluene, para

13.3

12.5

Cresol, meta

2.5

20.8

Cyclohexanol

2.9

24.3

Cyclohexane

9.8

12.9

Dibromomethane

12.7

15.8

Dichloroethane

13.2

12.2

Dichloromethane

14.6

8.9

Diethyl ketone

13.5

9.2

Diethyl oxalate

11.0

16.4

Diethylene glycol

5.0

24.7

Diphenyl

12.0

18.3

Dipropyl ether

13.2

8.6

Dipropyl oxalate

10.3

17.7

Ethyl acetate

13.7

9.1

Ethyl acrylate

12.7

10.4

Ethyl alcohol, 100%

10.5

13.8

Ethyl alcohol, 95%

9.8

14.3

Ethyl alcohol, 40%

6.5

16.6

Ethyl benzene

13.2

11.5

Ethyl bromide

14.5

8.1

2-Ethyl butyl acrylate

11.2

14.0

Ethyl chloride

14.8

6.0

Ethyl ether

14.5

5.3

Ethyl formate

14.2

8.4

2-Ethyl hexyl acrylate

9.0

15.0

Ethyl iodide

14.7

10.3

Ethyl propionate

13.2

9.9

Ethyl propyl ether

14.0

7.0

Ethyl sulfide

13.8

8.9

Ethylene bromide

11.9

15.7

Ethylene chloride

12.7

12.2

Ethylene glycol

6.0

23.6

Ethylidene chloride

14.1

8.7

Fluorobenzene

13.7

10.4

Formic acid

10.7

15.8

Freon-11

14.4

9.0

Freon-12

16.8

5.6

Freon-21

15.7

7.5

Freon-22

17.2

4.7

Freon-113

12.5

11.4

Glycerol, 100%

2.0

30.0

Glycerol, 50%

6.9

19.6

Heptane

14.1

8.4

Hexane

14.7

7.0

Hydrochloric acid, 31.5%

13.0

16.6

Iodobenzene

12.8

15.9

Isobutyl alcohol

7.1

18.0

Isobutyric acid

12.2

14.4

Isopropyl alcohol

8.2

16.0

Isopropyl bromide

14.1

9.2

Isopropyl chloride

13.9

7.1

Isopropyl iodide

13.7

11.2

Kerosene

10.2

16.9

Linseed oil, raw

7.5

27.2

Mercury

18.4

16.4

Methanol, 100%

12.4

10.5

Methanol, 90%

12.3

11.8

Methanol, 40%

7.8

15.5

Methyl acetate

14.2

8.2

Methyl acrylate

13.0

9.5

Methyl r-butyrate

12.3

9.7

Methyl n-butyrate

13.2

10.3

Methyl chloride

15.0

3.8

Methyl ethyl ketone

13.9

8.6

Methyl formate

14.2

7.5

Methyl iodide

14.3

9.3

Methyl propionate

13.5

9.0

Methyl propyl ketone

14.3

9.5

Methyl sulfide

15.3

6.4

Naphthalene

7.9

18.1

Nitric acid

12.8

13.8

Nitric acid, 60%

10.8

17.0

Nitrobenzene

10.6

16.2

Nitrogen dioxide

12.9

8.6

Nitrotoluene

11.0

17.0

Octane

13.7

10.0

Octyl alcohol

6.6

21.1

Pentachloroethane

10.9

17.3

Pentane

14.9

5.2

Phenol

6.9

20.8

Phosphorus tribromide

13.8

16.7

Phosphorus trichloride

16.2

10.9

Propionic acid

12.8

13.8

Propyl acetate

13.1

10.3

Propyl alcohol

9.1

16.5

Propyl bromide

14.5

7.5

Propyl chloride

14.4

7.5

Propyl formate

13.1

9.7

Propyl iodide

14.1

11.6

Sodium

16.4

13.9

Sodium hydroxide, 50%

3.2

25.8

Stannic chloride

13.5

12.8

Succinonitrile

10.1

20.8

Sulfur dioxide

15.2

7.1

Sulfuric acid, 110%

7.2

27.4

Sulfuric acid, 100%

8.0

25.1

Sulfuric acid, 98%

7.0

24.8

Sulfuric acid, 60%

10.2

21.3

Sulfuryl chloride

15.2

12.4

Tetrachloroethane

11.9

15.7

Thiophene

13.2

11.0

Titanium tetrachloride

14.4

12.3

Toluene

13.7

10.4

Trichloroethylene

14.8

10.5

Triethylene glycol

4.7

24.8

Turpentine

11.5

14.9

Vinyl acetate

14.0

8.8

Vinyl toluene

13.4

12.0

Water

10.2

13.0

Xylene, ortho

13.5

12.1

Xylene, meta

13.9

10.6

Xylene, para

13.9

10.9

Source:  Perry, R.H. and Green, D.W. (eds.), Perry’s Chemical Engineers’ Handbook, 7th edn., McGraw-Hill, New York, 1997. With permission.

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FIGURE A.4 Nomograph for viscosities of liquids at 1 atm. See Table A.1 for coordinates. (To convert centipoise to pascal-seconds, multiply by 0.001.)

TABLE A.2
The Viscosity of Water at 0°C–100°C

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Table entries were calculated from the following empirical relationships from measurements in viscometers calibrated with water at 20°C (and 1 atm), modified to agree with the currently accepted value for the viscosity at 20°C of 1.002 cP:

0°C20°C:log10ηT=1301998.333+8.1855(T20)+0.00585(T20)23.30233 (Hardy and Cottingham, 1949)

20°100°C:log10μTμ20=1.3272(20T)0.001053(T20)2T+105(J.F. Swindells, NBS, unpublished results)

TABLE A.3
Physical Properties of Ordinary Water and Common Liquids (SI Units)

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TABLE A.4
Physical Properties of Ordinary Water and Common Liquids (EE Unitsa)

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a  EE, English engineering.

TABLE A.5
Physical Properties of SAE Oils and Lubricants

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a  EE, English engineering.

TABLE A.6
Viscosity of Steam and Watera

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a  Values directly below underscored viscosities are for water.

b  Critical point.

TABLE A.7
Viscosities of Gasesa (Coordinates Apply to Figure A.5)

Gas

X

Y

μ × 107 (P)

Acetic acid

7.0

14.6

825 (50°C)

Acetone

8.4

13.2

735

Acetylene

9.3

15.5

1017

Air

10.4

20.4

1812

Ammonia

8.4

16.0

1000

Amylene (β)

8.6

12.2

676

Argon

9.7

22.6

2215

Arsine

8.6

20.0

1575

Benzene

8.7

13.2

746

Bromine

8.8

19.4

1495

Butane (η)

8.6

13.2

735

Butane (iso)

8.6

13.2

744

Butyl acetate (iso)

5.7

16.3

778

Butylene (α)

8.4

13.5

761

Butylene (β)

8.7

13.1

746

Butylene (iso)

8.3

13.9

786

Butyl formate (iso)

6.6

16.0

840

Cadmium

7.8

22.5

5690 (500)

Carbon dioxide

8.9

19.1

1463

Carbon disulfide

8.5

15.8

990

Carbon monoxide

10.5

20.0

1749

Carbon oxysulfide

8.2

17.9

1220

Carbon tetrachloride

8.0

15.3

966

Chlorine

8.8

18.3

1335

Chloroform

8.8

15.7

1000

Cyanogen

8.2

16.2

1002

Cyclohexane

9.0

12.2

701

Cyclopropane

8.3

14.7

870

Deuterium

11.0

16.2

1240

Diethyl ether

8.8

12.7

730

Dimethyl ether

9.0

15.0

925

Diphenyl ether

8.6

10.4

610 (50)

Diphenyl methane

8.0

10.3

605 (50)

Ethane

9.0

14.5

915

Ethanol

8.2

14.5

835

Ethyl acetate

8.4

13.4

743

Ethyl chloride

8.5

15.6

987

Ethylene

9.5

15.2

1010

Ethyl propionate

12.0

12.4

890

Fluoride

7.3

23.8

2250

Freon-11

8.6

16.2

1298 (93)

Freon-12

9.0

17.4

1496 (93)

Freon-14

9.5

20.4

1716

Freon-21

9.0

16.7

1389 (93)

Freon-22

9.0

17.7

1554 (93)

Freon-113

11.0

14.0

1166 (93)

Freon-114

9.4

16.4

1364 (93)

Helium

11.3

20.8

1946

Heptane (n)

9.6

10.6

618 (50)

Hexane (n)

8.4

12.0

644

Hydrogen

11.3

12.4

880

Hydrogen–helium

 10% H2, 90% He

11.0

20.5

1780 (0)

 25% H2, 75% He

11.0

19.4

1603 (0)

 40% H2, 60% He

10.7

18.4

1431 (0)

 60% H2, 40% He

10.8

16.7

1227 (0)

 81% H2, 19% He

10.5

15.0

1016 (0)

Hydrogen–sulfur dioxide

8.7

18.1

1259 (17)

 10% H2, 90% SO2

8.7

18.1

1259 (17)

 20% H2, 80% SO2

8.6

18.2

1277 (17)

 50% H2, 50% SO2

8.9

18.3

1332 (17)

 80% H2, 20% SO2

9.7

17.7

1306 (17)

Hydrogen bromide

8.4

21.6

1843

Hydrogen chloride

8.5

19.2

1425

Hydrogen cyanide

7.1

14.5

737

Hydrogen iodide

8.5

21.5

1830

Hydrogen sulfide

8.4

18.0

1265

Iodine

8.7

18.7

1730 (100)

Krypton

9.4

24.0

2480

Mercury

7.4

24.9

4500 (200)

Mercury bromide

8.5

19.0

2253

Mercuric chloride

7.7

18.7

2200 (200)

Mercuric iodide

8.4

18.0

2045 (200)

Mesitylene

9.5

10.2

660 (50)

Methane

9.5

15.8

1092

Methane (deuterated)

9.5

17.6

1290

Methanol

8.3

15.6

935

Methyl acetate

8.4

14.0

870 (50)

Methyl acetylene

8.9

14.3

867

3-Methyl-1-butene

8.0

13.3

716

Methyl butyrate (iso)

6.6

15.8

824

Methyl bromide

8.1

18.7

1327

Methyl bromide

8.1

18.7

1327

Methyl chloride

8.5

16.5

1062

3-Methylene-1-butene

8.0

13.3

716

Methylene chloride

8.5

15.8

989

Methyl formate

5.1

18.0

923

Neon

11.1

25.8

3113

Nitric oxide

10.4

20.8

1899

Nitrogen

10.6

20.0

1766

Nitrous oxide

9.0

19.0

1460

Nonane (n)

9.2

8.9

554 (50)

Octane (n)

8.8

9.8

586 (50)

Oxygen

10.2

21.6

2026

Pentene (n)

8.5

12.3

668

Pentane (iso)

8.9

12.1

685

Phosphene

8.8

17.0

1150

Propane

8.9

13.5

800

Propanol (n)

8.4

13.5

770

Propanol (iso)

8.4

13.6

774

Propyl acetate

8.0

14.3

797

Propylene

8.5

14.4

840

Pyridine

8.6

13.3

830 (50)

Silane

9.0

16.8

1148

Stannic chloride

9.1

16.0

1330 (100)

Stannic bromide

9.0

16.7

142 (100)

Sulfur dioxide

8.4

18.2

1250

Thiazole

10.0

14.4

958

Thiophene

8.3

14.2

901 (50)

Toluene

8.6

12.5

686

2,2,3-Trimethylbutane

10.0

10.4

691 (50)

Trimethylethane

8.0

13.0

686

Water

8.0

16.0

1250 (100)

Xenon

9.3

23.0

2255

Zinc

8.0

22.0

5250 (500)

Source:  Perry, R.H. and Green, D.W. (eds.), Perry’s Chemical Engineers’ Handbook, 7th edn., McGraw-Hill, New York, 1997. With permission.

a  Viscosity at 20°C unless otherwise indicated.

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FIGURE A.5 Nomograph for determining the absolute viscosity of a gas near ambient pressure and the relative viscosity of a gas compared with air. (Coordinates from Table A.7.) To convert from poise to pascal-seconds, multiply by 0.1. (From Beerman, Meas. Control., June 1982, 154–157.)

A.1 VISCOSITIES OF GASES AND LIQUIDS

The curves for hydrocarbon vapors and natural gases in the chart at the upper right are taken from Maxwell, and the curves for all other gases (except helium) in the chart are based upon Sutherland’s formula, as follows:

μ=μ0(0.555T0C0.555T+C)(TT0)3/2

where

μ is the viscosity in cP at temperature T

μ0 is the viscosity in cP at temperature T0

T is the absolute temperature, in °R (460 + °F), for which viscosity is desired

T0 is the absolute temperature, in °R, for which viscosity is known

C is Sutherland’s constant

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FIGURE A.6 Viscosity of (a) gases.

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FIGURE A.6 Viscosity of (a) gases. (b) refrigerant vapors. (From Crane Technical Paper 410, Crane Co., Chicago, IL, 1991.)

Note: The variation of viscosity with pressure is small for most gases. For gases given on this page, the correction of viscosity for pressure is less than 10% for pressures up to 500 psi.

Fluid

Approximate Values of C

O2

127

Air

120

N2

111

CO2

240

CO

118

SO2

416

NH3

370

H2

72

Example (Figure A.6a): The viscosity of sulfur dioxide gas (SO2) at 200°F is 0.016 cP.

Example (Figure A.6b): The viscosity of carbon dioxide gas (CO2) at about 80°F is 0.015 cP.

REFERENCES

Brown, G.G. et al., Unit Operations, Wiley, New York, 1951, p. 586.

Crane Company, Crane Technical Paper 410, Crane Co., Chicago, IL, 1991.

Hardy, R.C. and R.L. Cottingham, Viscosity of Water at T −20 to 150°C, J. Res. NBS, 42, 573, 1949.

Perry, R.H. and Green, D.W. (eds.), Perry’s Chemical Engineers’ Handbook, 7th edn., McGraw-Hill, New York, 1997.

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