Viscosity Conversion for Newtonian Fluids

(25°C, Sp. Gr. = 1)

 

POISE

STOKES

#4 FORD CUP

ZAHN

GARDNER HOLT

KREBS STORMER

#2

#3

#4

0.01

0.01

 

 

 

 

A-5

 

0.1

0.1

 

16

 

 

A-4

 

0.15

0.15

 

17

 

 

A-3

 

0.22

0.22

13.6

19

 

 

A-2

 

0.32

0.32

15.3

20

 

 

A-1

 

0.5

0.5

19

22

 

 

A

 

0.65

0.65

22

27

 

 

B

 

0.85

0.85

27

34

 

 

C

 

1

1

30

41

12

 

D

 

1.25

1.25

36

49

14

11

E

 

1.4

1.4

40

58

16

13

F

 

1.65

1.65

46

66

18

14

G

 

2

2

50

82

23

17

H

 

2.25

2.25

55

 

25

18

I

52

2.5

2.5

68

 

27

20

J

54

2.75

2.75

74

 

32

22

K

59

3

3

81

 

34

24

L

61

3.2

3.2

86

 

36

25

M

62

3.4

3.4

91

 

39

26

N

63

3.7

3.7

99

 

41

28

O

64

4

4

107

 

46

30

P

65

4.35

4.35

116

 

50

33

Q

66

4.7

4.7

125

 

52

34

R

67

5

5

133

 

57

37

S

68

5.5

5.5

146

 

63

40

T

69

6.3

6.3

167

 

68

44

U

71

8.85

8.85

199

 

 

64

V

78

10.7

10.7

270

 

 

 

W

85

12.9

12.9

 

 

 

 

X

85

17.6

17.6

 

 

 

 

Y

100

22.7

22.7

 

 

 

 

Z

105

27

27

 

 

 

 

Z-1

114

36.2

36.2

 

 

 

 

Z-2

129

46.3

46.3

 

 

 

 

Z-3

126

63.4

63.4

 

 

 

 

Z-4

 

98.5

98.5

 

 

 

 

Z-5

 

148

 

 

 

 

 

Z-6

 

 

 

 

 

 

 

 

 

 

NOTE: This chart is intended for use in comparing methods of relative viscosity measurements made on Newtonian liquids to absolute and kinematic viscosity. Assumes density is equal to 1.


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