Soap Bubble gets smaller and smaller !

At t = 0 t=0 , a spherical soap bubble with surface tension T and radius R is formed at one end of a cylindrical pipe of length L and cross-section radius of r o { r }_{ o } . The other end of the pipe is kept open to the atmosphere as shown.
The air that is inside the soap bubble has density ρ \rho , and coefficient of viscosity η \eta .

Find the time taken for the radius of the sphere to be halved . The time can be expressed as :

t = a b ( η L ρ c R d T ( r o ) e ) . \displaystyle{t\quad =\cfrac { a }{ b } (\cfrac { \eta L{ \rho }^{ c }{ R }^{ d } }{ T{ { (r }_{ o }) }^{ e } } )}.

Compute the Value of a + b + c + d + e a+b+c+d+e .

Here a , b , c , d , e a,b,c,d,e are non-negative integers.

Assumptions
\bullet R > > r o \displaystyle{R\quad >>\quad { r }_{ o }} .
\bullet Outside The Soap Bubble air is present in atmosphere with constant atmospheric Pressure (1 atm)
\bullet Surface Tension is Enough So that It always Maintains the spherical Shape of the Soap bubble!
\bullet Length of Pipe is not So long (i.e Initial Volume Capacity of sphere is Sufficiently greater Than that of Pipe )

This is Part of my Set Deepanshu's Mechanics Blast


The answer is 31.

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3 solutions

Deepanshu Gupta
Jan 5, 2015

Let at time t=t let radius of bubble is 'r'

Volume Flow out through tube is : (Use Poiseuille Law for Volume Rate flow through pipes)

d V d t = Δ P ( π r o 4 ) 8 η L ( 1 ) \displaystyle{\cfrac { dV }{ dt } =\cfrac { \Delta P(\pi { { r }_{ o } }^{ 4 }) }{ 8\eta L } \quad (1)} .

Also Volume that flow out through Spherical soap bubble decrees , and equal to volume rate flow through Pipe (Using continuity theorem)

Δ P = 4 T r ( 2 ) d V d t = 4 π r 2 ( d r d t ) ( 3 ) \displaystyle{\because \Delta P=\cfrac { 4T }{ r } \quad (2)\\ \cfrac { dV }{ dt } =4\pi r^{ 2 }(\cfrac { -dr }{ dt } )\quad (3)\\ } .

Using Continuity Theorem : 4 π r 2 d r d t = 4 T ( π r o 4 ) 8 η L r R R / 2 r 3 d r = T ( π r o 4 ) 8 η L 0 T d t \displaystyle{-4\pi r^{ 2 }\cfrac { dr }{ dt } =\cfrac { 4T(\pi { { r }_{ o } }^{ 4 }) }{ 8\eta Lr } \\ \\ -\int _{ R }^{ R/2 }{ r^{ 3 }dr } =\cfrac { T(\pi { { r }_{ o } }^{ 4 }) }{ 8\eta L } \int _{ 0 }^{ T }{ dt } } .

we get : T = 15 8 ( η L R 4 T ( r o ) 4 ) \boxed { { T\quad =\cfrac { 15 }{ 8 } (\cfrac { \eta L{ R }^{ 4 } }{ T{ { (r }_{ o }) }^{ 4 } } ) } } .

Nice problem! A simple application of Poiseuille's law!

Sumanth R Hegde - 4 years, 1 month ago

Did the same!!!! Awesome question.

A Former Brilliant Member - 4 years, 5 months ago

@Deepanshu Gupta How is the assumption R > > r 0 R > > r_{0} important? Please help me out with it.

Ankit Kumar Jain - 3 years, 3 months ago
Mahathir Ahmad
Dec 31, 2014

This is an interesting problem. I will give some hints:

  1. Use Poiseuille law on the cylindrical pipe.

  2. Try to find the excess pressure on the sphere in terms of surface tension and radius of sphere.

  3. Express the volumetric flow rate in the Poiseuille law in terms of the change in radius with respect to time.

4.Substitute the value for pressure loss , integrate the equation and you have the answer.

Do we need the density ???

I got it right without using it.

Santanu Banerjee - 6 years, 5 months ago

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Actually Not , But I added it So that every one Thinks That why or why not , Here Bernouili Principle is not applicable ! (And I specifically Mention That a,b,c,d,e all are Non-negative Integer , obviously zero is one of them )

Answer is t = 15 8 ( η L R 4 T ( r o ) 4 ) \boxed { { t\quad =\cfrac { 15 }{ 8 } (\cfrac { \eta L{ R }^{ 4 } }{ T{ { (r }_{ o }) }^{ 4 } } ) } } .

Deepanshu Gupta - 6 years, 5 months ago

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Can you please post a solution, I'm not able to get the 15 / 8 15/8 value...Can you help??

A Former Brilliant Member - 6 years, 5 months ago

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@A Former Brilliant Member @Upanshu Gypta @Abhineet Nayyar I had Posted my solution

Deepanshu Gupta - 6 years, 5 months ago

Yeah!! I'm getting 15/64

Kunal Gupta - 6 years, 5 months ago
Rishav Koirala
Mar 13, 2015

The important point is to notice that the rate does not depend on the density whatsoever and then apply Poiseuille's volume flux equation with a little calculus.

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