Ratio Ratio Fluid kg/(m - s) μμ (H) kg/m m/s vlv(Hg) Hydrogen Air 9.0 E-6 1.0 0.084 1.05 E-4 910 1.8 E-5 2.1 1.20 1.50 E-5 130 Gasoline Water Ethyl alcohol Mercury 2.9 E-4 33 680 4.22 E-7 3.7 114 135 1.0 E-3 998 1.01 E-6 8.7 1.2 E-3 789 1.52 E-6 13 1.5 E-3 170 13,550 1.16 E-7 1.0 SAE 30 oil 0.29 33,000 170,000 891 1,260 3.25 E-4 2,850 10,300 Glycerin 1.5 1.18 E-3 '1 kg/(m - s) = 0.0209 slug/(ft - s); 1 m/s = 10.76 f/s. 10 · Liquid- 6. 4 Dense gas Two-phase region 25 2. 10 Hi=# Critical point 3 0.8 0.7 0.5 0.6 0.5 P, = p/P = 0.2 0.4 Low-density limit 10 0.3 of 0.2 0.4 5 6 7 8910 0.6 0.8 1 4 T= 2.
Ratio Ratio Fluid kg/(m - s) μμ (H) kg/m m/s vlv(Hg) Hydrogen Air 9.0 E-6 1.0 0.084 1.05 E-4 910 1.8 E-5 2.1 1.20 1.50 E-5 130 Gasoline Water Ethyl alcohol Mercury 2.9 E-4 33 680 4.22 E-7 3.7 114 135 1.0 E-3 998 1.01 E-6 8.7 1.2 E-3 789 1.52 E-6 13 1.5 E-3 170 13,550 1.16 E-7 1.0 SAE 30 oil 0.29 33,000 170,000 891 1,260 3.25 E-4 2,850 10,300 Glycerin 1.5 1.18 E-3 '1 kg/(m - s) = 0.0209 slug/(ft - s); 1 m/s = 10.76 f/s. 10 · Liquid- 6. 4 Dense gas Two-phase region 25 2. 10 Hi=# Critical point 3 0.8 0.7 0.5 0.6 0.5 P, = p/P = 0.2 0.4 Low-density limit 10 0.3 of 0.2 0.4 5 6 7 8910 0.6 0.8 1 4 T= 2.
Elements Of Electromagnetics
7th Edition
ISBN:9780190698614
Author:Sadiku, Matthew N. O.
Publisher:Sadiku, Matthew N. O.
ChapterMA: Math Assessment
Section: Chapter Questions
Problem 1.1MA
Related questions
Question
Knowing μ for air at 20 ° C from Table 1.4, estimate its
viscosity at 500 ° C by ( a ) the power law and ( b ) the Sutherland
law. Also make an estimate from ( c ) Fig. 1.6. Compare
with the accepted value of μ ≈ 3.58 E-5 kg/m ∙ s.
![Ratio
Ratio
Fluid
kg/(m - s)
μμ (H)
kg/m
m/s
vlv(Hg)
Hydrogen
Air
9.0 E-6
1.0
0.084
1.05 E-4
910
1.8 E-5
2.1
1.20
1.50 E-5
130
Gasoline
Water
Ethyl alcohol
Mercury
2.9 E-4
33
680
4.22 E-7
3.7
114
135
1.0 E-3
998
1.01 E-6
8.7
1.2 E-3
789
1.52 E-6
13
1.5 E-3
170
13,550
1.16 E-7
1.0
SAE 30 oil
0.29
33,000
170,000
891
1,260
3.25 E-4
2,850
10,300
Glycerin
1.5
1.18 E-3
'1 kg/(m - s) = 0.0209 slug/(ft - s); 1 m/s = 10.76 f/s.](/v2/_next/image?url=https%3A%2F%2Fcontent.bartleby.com%2Fqna-images%2Fquestion%2Fc4f346a2-ee8b-45ce-b156-c11b3f8a9a4b%2F355913b0-2157-4296-9957-3e0295b30cd7%2Fo8v60wma.png&w=3840&q=75)
Transcribed Image Text:Ratio
Ratio
Fluid
kg/(m - s)
μμ (H)
kg/m
m/s
vlv(Hg)
Hydrogen
Air
9.0 E-6
1.0
0.084
1.05 E-4
910
1.8 E-5
2.1
1.20
1.50 E-5
130
Gasoline
Water
Ethyl alcohol
Mercury
2.9 E-4
33
680
4.22 E-7
3.7
114
135
1.0 E-3
998
1.01 E-6
8.7
1.2 E-3
789
1.52 E-6
13
1.5 E-3
170
13,550
1.16 E-7
1.0
SAE 30 oil
0.29
33,000
170,000
891
1,260
3.25 E-4
2,850
10,300
Glycerin
1.5
1.18 E-3
'1 kg/(m - s) = 0.0209 slug/(ft - s); 1 m/s = 10.76 f/s.
![10
· Liquid-
6.
4
Dense gas
Two-phase
region
25
2.
10
Hi=#
Critical
point
3
0.8
0.7
0.5
0.6
0.5
P, = p/P = 0.2
0.4
Low-density limit
10
0.3
of
0.2
0.4
5 6 7 8910
0.6
0.8 1
4
T=
2.](/v2/_next/image?url=https%3A%2F%2Fcontent.bartleby.com%2Fqna-images%2Fquestion%2Fc4f346a2-ee8b-45ce-b156-c11b3f8a9a4b%2F355913b0-2157-4296-9957-3e0295b30cd7%2Fwlobcpg.png&w=3840&q=75)
Transcribed Image Text:10
· Liquid-
6.
4
Dense gas
Two-phase
region
25
2.
10
Hi=#
Critical
point
3
0.8
0.7
0.5
0.6
0.5
P, = p/P = 0.2
0.4
Low-density limit
10
0.3
of
0.2
0.4
5 6 7 8910
0.6
0.8 1
4
T=
2.
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