Question

A spherical raindrop 3.1 mm in diameter falls through a vertical distance of 3550 m. Take...

A spherical raindrop 3.1 mm in diameter falls through a vertical distance of 3550 m. Take the cross-sectional area of a raindrop = πr2, drag coefficient = 0.45, density of water to be 1000 kg/m3,and density of air to be 1.2 kg/m3.

(a) Calculate the speed a spherical raindrop would achieve falling from 3550 m in the absence of air drag.

(b) What would its speed be at the end of 3550 m when there is air drag?

Homework Answers

Answer #1

According to the given problem,

Volume of spherical raindrop = 4/3π r3 = 0.0156 cm3 and mass = 0.0156 gm

a) Speed in the absence of air drag.

S = 1/2 g t2

t2 = 2 S / g = 3550 * 2 / 9.81 = 723.75

t = 26.9 s

v = g * t = 9.81 * 26.9 = 263.9 m/s

v = 264 m/s

b)

Vt = √2 m g / Cρair A
A = πr2 = π(1.55*10-3)2 = 7.55*10-6 m2
m = 0.0156 gm = 0.0156*10-3 kg
g = 9.81
C = 0.45
ρair = 1.2 kg /m3

vt = 8.66 m/s.

I hope you understood the problem, If yes rate me!! or else comment for a better solution.

Know the answer?
Your Answer:

Post as a guest

Your Name:

What's your source?

Earn Coins

Coins can be redeemed for fabulous gifts.

Not the answer you're looking for?
Ask your own homework help question
Similar Questions
A spherical raindrop 2.9 mm in diameter falls through a vertical distance of 3950 m. Take...
A spherical raindrop 2.9 mm in diameter falls through a vertical distance of 3950 m. Take the cross-sectional area of a raindrop = πr2, drag coefficient = 0.45, density of water to be 1000 kg/m3,and density of air to be 1.2 kg/m3. (a) Calculate the speed (in m/s) a spherical raindrop would achieve falling from 3950 m in the absence of air drag. 278.222 m/s (b) What would its speed (in m/s) be at the end of 3950 m when...
Calculate the speed (in m/s) a spherical rain drop would achieve falling from 2.10 km in...
Calculate the speed (in m/s) a spherical rain drop would achieve falling from 2.10 km in the absence of air drag and with air drag. Take the size across of the drop to be 9 mm, the density to be 1.00 ✕ 103 kg/m3, and the surface area to be πr2. (Assume the density of air is 1.21 kg/m3.) (a) in the absence of air drag 202.985  m/s (correct) (b) with air drag 9.8687 m/s (incorrect)
Calculate the velocity a spherical rain drop would achieve falling (taking downward as positive) from 4.2...
Calculate the velocity a spherical rain drop would achieve falling (taking downward as positive) from 4.2 km in the following situations. h = 4.2 km l = 4.8 mm d = 1.23 kg/m3 a Calculate the velocity in the absence of air drag in m/s. b  Calculate the velocity with air drag in m/s. Take the size across of the drop to be 4.8 mm, the density of air to be 1.23 kg/m3, the density of water to be 1000 kg/m3,...
Calculate the speed (in m/s) a spherical rain drop would achieve falling from 4.10 km in...
Calculate the speed (in m/s) a spherical rain drop would achieve falling from 4.10 km in the absence of air drag and with air drag. Take the size across of the drop to be 5 mm, the density to be 1.00 ? 103 kg/m3, and the surface area to be ?r2. (Assume the density of air is 1.21 kg/m3.) (a)in the absence of air drag. (b) with air drag.
Calculate the speed a spherical rain drop would achieve falling from 4.2 km (a) in the...
Calculate the speed a spherical rain drop would achieve falling from 4.2 km (a) in the absence of air drag (b) with air drag. Take the size across of the drop to be 4.2 mm, the density to be 1.00×103??/?3 , and the surface area to be ??2 . Additionaly: the density of air is 1.21??/?3 , and the drag coefficient for the spherical drop is 0.45. a) In the absence of air drag b) with air drag
A 5 kg cylinder of diameter (Di) 100 mm and length (L) 200 mm falls through...
A 5 kg cylinder of diameter (Di) 100 mm and length (L) 200 mm falls through a lubricated bearing of diameter (Do) 101 mm. If the cylinder is falling at a terminal velocity of 1.5 m/s determine the absolute viscosity oil of the oil surrounding the sides of the cylinder.
Air is injected into a 50 m long horizontal pipeline (of 42 mm diameter) carrying a...
Air is injected into a 50 m long horizontal pipeline (of 42 mm diameter) carrying a clay slurry of density 1452 kg/m 3 . The rheological behaviour of the slurry follows the power-law model, with m = 5.55 Pa sn and n = 0.35. The volumetric flow rates of air and liquid are 7.48 and 1.75 m3 /h, respectively. The air is introduced into the pipeline at 20°C and at a pressure of 1.2 bar. Ascertain the flow pattern occurring...
3a. If a typical cherry pit is spherical, with 4 mm diameter, what is the fastest...
3a. If a typical cherry pit is spherical, with 4 mm diameter, what is the fastest speed it can be spat out before it is expected to set up turbulent air flows around it, thereby making its trajectory less efficient? The viscosity of air with density 1.1 kg/m3 is 0.00002 N-s/m2 . 3b. If a much smaller pit is found, one with half the diameter of the first, how much faster can IT now be spat before turbulent flow is...
Dust grains of diameter 0.83 µm and density 1000 kg/m3 are in equilibrium with air (A...
Dust grains of diameter 0.83 µm and density 1000 kg/m3 are in equilibrium with air (A = 28.9) at a temperature of 278 K . What is the rms speed of the dust particles? 1 m = 106µm. Answer in units of mm/s.
A cylindrical fluidized bed of diameter 0.5 m is used in flour mill for flour production....
A cylindrical fluidized bed of diameter 0.5 m is used in flour mill for flour production. Air of density 1.2 kg/m3 and viscosity 1.84 x 10-5 Pa.s is fluidizing the flour powder of mean sieve size 60 µm and particle density 1800 kg/m3 . 240 kg of flour powder is charged to the bed and air flowrate to the bed is 140 m3 /hr. The average bed voidage at incipient fluidization is 0.45. Compute the following problems: (a) the minimum...