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Authors: Philip J. Pritchard, John W. Mitchell Published: Wiley 2015 Edition: 9th Pages: 1190 Type: pdf Size: 54MB
Typology: Cheat Sheet
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Tar Sand
“Silly Putty” Jello
Modeling clay Toothpaste
Wax Shaving cream
Some of these substances exhibit characteristics of solids and fluids under different conditions.
pressures or over long periods, they exhibit fluid characteristics. At higher temperatures, all three
liquefy and become viscous fluids.
Modeling clay and silly putty show fluid behavior when sheared slowly. However, they fracture
under suddenly applied stress, which is a characteristic of solids.
Toothpaste behaves as a solid when at rest in the tube. When the tube is squeezed hard, toothpaste
“flows” out the spout, showing fluid behavior. Shaving cream behaves similarly.
Sand acts solid when in repose (a sand “pile”). However, it “flows” from a spout or down a steep
incline.
a. Conservation of mass — The mass of a system is constant by definition.
b. Newton's second law of motion — The net force acting on a system is directly proportional to the product of the
system mass times its acceleration.
c. First law of thermodynamics — The change in stored energy of a system equals the net energy added to the
system as heat and work.
d. Second law of thermodynamics — The entropy of any isolated system cannot decrease during any process
between equilibrium states.
e. Principle of angular momentum — The net torque acting on a system is equal to the rate of change of angular
momentum of the system.
The given or available data is:
D = 16 ⋅ft p = 1000 ⋅psi T = (77 + 460)⋅R T = 537 ⋅R
For oxygen the critical temperature and pressure are: (^) Tc = 279 ⋅R pc = 725.2⋅psi (data from NIST WebBook)
so the reduced temperature and pressure are:
Using a compressiblity factor chart: (^) Z = 0.948 Since this number is close to 1, we can assume ideal gas behavior.
Therefore, the governing equation is the ideal gas equation (^) p = ρ⋅RO2⋅T (^) and (^) ρ = M V
where V is the tank volume (^) V = π⋅D^3 6
V = π^ × (16⋅ ft) 3 6
V = 2144.7⋅ ft^3
Hence:
The data provided are: (^) M = 1 × 10 −^13 ⋅slug Vt 0.2 ft s
Newton's 2nd law for the general motion is (ignoring buoyancy effects) (^) M dV dt
⋅ = M g⋅ −k V⋅ (1)
Newton's 2nd law for the steady state motion becomes (ignoring buoyancy effects) (^) M g⋅ = k V⋅ t so (^) k M g⋅ Vt
k 1 × 10 −^13 ⋅ slug× 32.2 ft s^2
⋅ s 0.2 ft⋅
× lbf s
slug ft⋅
= × k 1.61 × 10 −^11 lbf s⋅ ft
dV g k M
To find the time to reach 99% of V (^) t , we need V ( t ). From 1, separating variables =^ dt
Integrating and using limits (^) t M k
− ln 1 k M g⋅
We must evaluate this when (^) V = 0.99 V⋅ t V 0.198 ft s
t − 1 × 10 −^13 ⋅ slug ft 1.61 × 10 −^11 ⋅ lbf⋅s
× lbf s
slug ft⋅
× ln 1 1.61 × 10 −^11 lbf s⋅ ft
1 × 10 −^13 ⋅slug
× s
2 32.2 ft⋅
× 0.198 ft⋅ s
× slug ft⋅ lbf s ⋅^2
t =0.0286 s
2
1
1
𝑅/𝑐𝑝
𝑅/𝑐𝑝
2
We must evaluate this when (^) V = 0.99 V⋅ t V 0.198 ft s
t 1 × 10 −^13 ⋅ slug ft 1.61 × 10 −^11 ⋅ lbf⋅s
× lbf s
slug ft⋅
⋅ ln 1 1.61 × 10 −^11 lbf s⋅ ft
1 × 10 −^13 ⋅slug
× s
2 32.2 ft⋅
× 0.198 ft⋅ s
× slug ft⋅ lbf s ⋅^2
t =0.0286 s
From 2, after rearranging (^) V dy dt
= M g⋅ k
1 e
k M
− ⋅t −
Integrating and using limits (^) y M g⋅ k
t M k
e
k M
− ⋅t − 1
y 1 × 10 −^13 ⋅ slug 32.2 ft⋅ s^2
× ft 1.61 × 10 −^11 ⋅ lbf⋅s
× lbf s
slug ft⋅
⋅ 0.0291 s⋅
10 −^13 ⋅ slug ft 1.61 × 10 −^11 ⋅ lbf⋅s
⋅ lbf s
slug ft⋅
⋅ e
1.61 10× −^11 1 10× −^13
− ⋅. − 1
y =4.49 × 10 −^3 ⋅ft
0 5 10 15 20 25
5
This plot can also be presented in Excel.
m^2
Treat the sky diver as a system; apply Newton's 2nd law:
Newton's 2nd law for the sky diver (mass M) is (ignoring buoyancy effects): (^) M dV dt
⋅ = M g⋅ −k V ⋅^2 (1)
(a) For terminal speed V (^) t , acceleration is zero, so M g⋅ − k V ⋅^2 = 0 so (^) Vt M g⋅ k
Vt 70 kg⋅ × 9.81m s^2
⋅ m
2
0.25 N⋅ ⋅s^2
× N s
kg ×m
1 2 = Vt 52.4 m s
(b) For V at y = 100 m we need to find V ( y ). From (1) M dV dt
⋅ M dV dy
⋅ dy dt
= ⋅ M V⋅ dV dt
= ⋅ =M g⋅ −k V ⋅^2
Separating variables and integrating:
0
V V V
1 k V
M g⋅
d 0
y g y
=⎮⌡ d
so (^) ln 1 k V
M g⋅
2 k⋅ M
= − y or^ V^2 M g⋅ k
1 e
2 k⋅ ⋅y M
− −
Hence (^) V y( ) Vt 1 e
2 k⋅ ⋅y M
− −
1 2
= ⋅
For y = 100 m: (^) V 100 m( ⋅ ) 52.4 m s
⋅ 1 e
− 2 × 0.25N s^ ⋅^2 m^2
⋅ × 100 ⋅m 1 70 kg⋅
× kg m⋅ s 2 ⋅N
× −
1 2
= ⋅ V 100 m( ⋅ ) 37.4 m s
ΣF (^) y = m dvdt= −mg , so v = v 0 – gt, and tf = 2t (^) v=0 = 2v 0 /g
Also, mv dv dy
mg, v dv g dy, 0 v 2
(^0) gh 2 = − = − − = −
Thus h = v 02 2g (1)
ΣF m du dt
0, so u u const, and R u t 2u v 0 0 f (^) g x =^ =^ =^ =^ =^ =^0 0 (2)
From Eq. 1: v 02 = 2gh (3)
From Eq. 2: u gR 2v
gR 2 2gh
u gR (^000) 8h
Then 2
2 1 0 2 2 02 20 0 8 2 and^28 ⎟⎟ ⎠
h gh V gh gR h V u v gR (4)
s
m 8 10 m^9.^81 s 2 9. 81 m^2
1 2 2 (^0 22) ⎟⎟⎠ =
From Eq. 3: v 2gh V sin sin
2gh (^0 0) V 1 0
θ 0
37.7m
10 m s s
sin 2 9. 81 m^2
1 2
Plots of V 0 = V 0 (h) (Eq. 4) and θ 0 = θ (^) 0(h) (Eq. 5) are presented below:
h (m)
(m/s) 0
h (m)
θ^
o^ (
3