Chapter 9 · Mechanical Properties of Fluids

9.3 Viscosity, Stokes' Law and Terminal Velocity

Real fluids resist sliding over themselves. This internal friction, measured by the coefficient of viscosity $\eta$, gives a small sphere a drag $6\pi\eta rv$ and makes falling drops and balls settle to a steady terminal velocity.

Tip a jar of honey and a glass of water at the same moment: the water is gone in a second, while the honey creeps out as a slow thick ribbon. Both are liquids of similar density, so gravity pulls them almost equally; what differs is how strongly each layer of liquid resists sliding over the next. That resistance is viscosity. It is why engines need oil of the right "grade", why blood pressure must push blood through narrow vessels, and why a cloud droplet drifts down at a centimetre a second instead of plummeting.

In Section 9.2 we ignored viscosity to get Bernoulli's principle. Here we put it back. You will define the coefficient of viscosity from the flow between two plates, meet Stokes' law for the drag on a small sphere, and use it to find the terminal velocity that a sphere reaches when the drag, the upthrust and its weight balance — the basis of the falling-ball viscometer and of every calculation about how fast dust, sediment and droplets settle.

Viscosity

Put a thin layer of liquid between a large fixed plate and a parallel plate that you drag along at constant speed $v$. The liquid touching each plate sticks to it (it has the plate's velocity), so the bottom layer is at rest and the top layer moves at $v$. In between, the liquid moves in thin layers, each sliding a little faster than the one below: this is laminar flow. To keep the top plate moving at constant speed you must keep pulling on it, because each layer drags back on the faster layer above it — a fluid version of friction.

Experiment shows that the force needed is proportional to the area $A$ of the plate and to the speed $v$, and inversely proportional to the thickness $l$ of the layer. In terms of shear (Chapter 8), the fluid is being sheared continuously, and the shear stress $\dfrac{F}{A}$ is proportional not to the shear strain but to the rate at which the strain grows, $\dfrac{v}{l}$.

📘 Definition 9.6 — Coefficient of viscosity

When layers of a fluid slide over each other in laminar flow, with the velocity changing by $dv$ across a distance $dx$ at right angles to the flow, the tangential (viscous) force on a layer of area $A$ is

$$F=\eta A\frac{dv}{dx}.$$

The constant $\eta$ is the coefficient of viscosity of the fluid; $\dfrac{dv}{dx}$ is the velocity gradient. For a layer of thickness $l$ between a fixed plate and a plate moving at $v$, the gradient is uniform and $F=\eta A\dfrac{v}{l}$, so

$$\eta=\frac{F/A}{v/l}=\frac{\text{shear stress}}{\text{rate of shear strain}}.$$

SI unit: $\text{N s/m}^2=\text{Pa s}$ (also called the poiseuille); the CGS unit is the poise, $1\ \text{poise}=0.1\ \text{Pa s}$. Dimensions $[\text{M L}^{-1}\text{T}^{-1}]$.

FluidTemperature$\eta$ (Pa s)
air$20\ ^\circ\text{C}$$1.8\times10^{-5}$
water$20\ ^\circ\text{C}$ / $100\ ^\circ\text{C}$$1.0\times10^{-3}$ / $0.28\times10^{-3}$
blood$37\ ^\circ\text{C}$about $2.7\times10^{-3}$
light machine oil$20\ ^\circ\text{C}$about $0.10$
castor oil$20\ ^\circ\text{C}$about $0.99$
glycerine$20\ ^\circ\text{C}$about $1.5$
honey$20\ ^\circ\text{C}$a few (varies widely)

The viscosity of a liquid falls steeply as it warms (warm honey pours easily, cold engine oil does not), because the molecules escape more easily from their neighbours' attraction. The viscosity of a gas, by contrast, rises with temperature: in a gas, momentum is carried between layers by molecules darting across, and hotter molecules dart faster. In a pipe, laminar flow is fastest along the axis and zero at the wall, where the fluid sticks; the velocity profile is a parabola, and a pressure difference along the pipe is needed to keep the flow going — Bernoulli's principle alone would say none is needed in a uniform horizontal pipe.

✏️ Example 1 — Sliding on a film of oil
A flat plate of area $0.10\ \text{m}^2$ is pulled at a steady $0.10\ \text{m/s}$ across a film of light machine oil ($\eta=0.10\ \text{Pa s}$) $0.50\ \text{mm}$ thick on a fixed flat surface. (a) Find the velocity gradient and the force needed. (b) What force is needed if the film is only $0.25\ \text{mm}$ thick? (c) At what rate is energy being dissipated in case (a)?
(a) $\dfrac{v}{l}=\dfrac{0.10}{5.0\times10^{-4}}=200\ \text{s}^{-1}$; $\ F=\eta A\dfrac vl=0.10\times0.10\times200=2.0\ \text{N}$.
(b) Half the thickness doubles the gradient: $F=4.0\ \text{N}$.
(c) $P=Fv=2.0\times0.10=0.20\ \text{W}$, turned into heat in the oil.
Check Units: $\text{Pa s}\times\text{m}^2\times\text{s}^{-1}=\text{Pa m}^2=\text{N}$ ✓. Unlike dry friction, the viscous force grows with speed and vanishes at zero speed. Interactive 1 starts here.
Interactive 1 — Layers of a Viscous Fluid

A plate of area $0.10\ \text{m}^2$ (top) is pulled over a fluid film resting on a fixed plate. The arrows show the velocity of each layer: zero at the bottom, $v$ at the top, a straight-line profile. Press Play: a vertical line of dye, drawn across the film, is sheared into a slope as the layers slide. Change the fluid, the speed and the thickness and read off the force $F=\eta Av/l$.

0.10 m/s0.50 mm
velocity gradient $v/l$—
shear stress $\eta v/l$—
force on the plate—
power dissipated $Fv$—

Critical velocity and Reynolds number. Laminar flow lasts only up to a certain speed, the critical velocity $v_c$ (Section 9.2); faster than that, eddies form and the flow becomes turbulent. Whether a flow is laminar is decided by a dimensionless combination, the Reynolds number

$$Re=\frac{\rho vd}{\eta},$$

where $\rho$ is the fluid's density, $v$ its speed and $d$ the diameter of the pipe. It compares the fluid's inertia ($\rho v$, which drives eddies) with viscosity (which damps them). For flow in a pipe, roughly: $Re\lt1000$ laminar, $Re\gt2000$ turbulent, unsteady in between. Setting $Re\approx2000$ gives $v_c\approx\dfrac{2000\,\eta}{\rho d}$: the critical velocity is high for viscous fluids and narrow tubes, low for dense, runny fluids in wide pipes. For water ($\eta=1.0\times10^{-3}\ \text{Pa s}$) in a $1.0\ \text{cm}$ pipe, $v_c\approx\dfrac{2000\times1.0\times10^{-3}}{1.0\times10^3\times0.010}=0.20\ \text{m/s}$ — which is why water from a tap opened wide comes out turbulent.

Stokes' law

A sphere moving slowly through a fluid drags the fluid near it along, setting up velocity gradients all round it, so it feels a viscous force opposing its motion. What can the force depend on? The viscosity $\eta$, the radius $r$ and the speed $v$ — at low speeds the fluid's density does not enter, because the inertia of the fluid is unimportant compared with viscosity. Dimensional analysis (Section 1.3) then fixes the form. Suppose $F=k\,\eta^ar^bv^c$. With $[\eta]=[\text{M L}^{-1}\text{T}^{-1}]$:

$$[\text{M L T}^{-2}]=[\text{M}]^a[\text{L}]^{-a+b+c}[\text{T}]^{-a-c}.$$

Comparing powers: $a=1$; $-a-c=-2$ gives $c=1$; $-a+b+c=1$ gives $b=1$. So $F=k\,\eta rv$. A full calculation of the flow round the sphere, beyond this course, gives $k=6\pi$.

📐 Result 9.9 — Stokes' law

A sphere of radius $r$ moving with speed $v$ relative to a fluid of viscosity $\eta$ experiences a viscous drag force opposite to its velocity, of magnitude

$$F=6\pi\eta rv ,$$

provided the flow round it is laminar (low speed, small sphere, viscous fluid) and the fluid extends far beyond the sphere on all sides.

The drag is proportional to the speed, like the viscous force between plates. For larger bodies or higher speeds (a cricket ball in air, a parachutist, a car) the flow behind the body becomes turbulent and the drag grows roughly as $v^2$ instead; Stokes' law then underestimates it badly.

Terminal velocity

Drop a small steel ball into a tall jar of glycerine. Three forces act on it: its weight downward, the upthrust (buoyancy) of the displaced liquid upward, and the viscous drag upward, opposing its downward motion. At first the ball is slow, the drag is small and it accelerates. As it speeds up the drag grows, the net force shrinks, and so does the acceleration. Soon the drag has grown until the forces balance; from then on the ball falls at a constant speed.

📘 Definition 9.7 — Terminal velocity

The terminal velocity of a body falling (or rising) through a fluid is the constant velocity it eventually reaches, when the net force on it — weight, upthrust and drag together — is zero, so its acceleration is zero.

For a sphere of radius $r$ and density $\rho$ falling through a fluid of density $\sigma$ and viscosity $\eta$, its weight is $\tfrac43\pi r^3\rho g$ and the upthrust is $\tfrac43\pi r^3\sigma g$. At the terminal velocity $v_t$ the Stokes drag balances their difference:

$$6\pi\eta rv_t=\tfrac43\pi r^3(\rho-\sigma)g .$$
📐 Result 9.10 — Terminal velocity of a small sphere

A small sphere of radius $r$ and density $\rho$ moving through a fluid of density $\sigma$ and viscosity $\eta$, with laminar flow round it (so that Stokes' law holds), reaches a terminal velocity of magnitude

$$v_t=\frac{2r^2(\rho-\sigma)g}{9\eta}.$$

It is downward if $\rho\gt\sigma$, and upward (the body rises) if $\rho\lt\sigma$ — an air bubble in a liquid. Note $v_t\propto r^2$: a sphere twice as wide falls four times as fast.

Once the terminal velocity is reached the kinetic energy no longer changes, so the gravitational potential energy lost (minus the work done by the upthrust) is all converted into heat in the fluid by the viscous force. A falling-ball viscometer turns Result 9.10 round: time a ball of known size and density falling between two marks, once it has reached its terminal velocity, and calculate $\eta=\dfrac{2r^2(\rho-\sigma)g}{9v_t}$.

✏️ Example 2 — Cloud droplets and drizzle
Take air to have $\eta=1.8\times10^{-5}\ \text{Pa s}$ and density $1.2\ \text{kg/m}^3$. (a) Find the terminal velocity of a cloud droplet of water of radius $10\ \mu\text{m}$. (b) What does Stokes' law predict for a drizzle drop of radius $0.10\ \text{mm}$? (c) Comment, given that measured drizzle drops of this size fall at about $0.7\ \text{m/s}$.
(a) $v_t=\dfrac{2(1.0\times10^{-5})^2(1000-1.2)(9.8)}{9(1.8\times10^{-5})}=\dfrac{1.96\times10^{-6}}{1.62\times10^{-4}}=1.2\times10^{-2}\ \text{m/s}$ — about $1\ \text{cm/s}$. The faintest air current keeps such droplets aloft, which is why clouds float.
(b) Ten times the radius, a hundred times the speed: $1.2\ \text{m/s}$.
(c) Stokes' law over-predicts by almost a factor of two: at $1\ \text{m/s}$ a $0.2\ \text{mm}$ drop is too big and too fast for the flow round it to stay laminar, so the drag is larger than $6\pi\eta rv$.
Check The air's density is less than $0.2\%$ of water's, so the upthrust hardly matters here; in a liquid it matters a great deal. Large raindrops reach only about $9\ \text{m/s}$ — not the $140\ \text{m/s}$ of free fall from a kilometre — because drag of any kind sets a terminal speed.
✏️ Example 3 — A steel ball in glycerine
A steel ball of radius $1.0\ \text{mm}$ and density $7.8\times10^3\ \text{kg/m}^3$ falls through glycerine of density $1.26\times10^3\ \text{kg/m}^3$ and viscosity $1.5\ \text{Pa s}$. Find (a) its terminal velocity, (b) the viscous force on it at that speed, and check that this force balances the weight minus the upthrust.
(a) $v_t=\dfrac{2(1.0\times10^{-3})^2(7800-1260)(9.8)}{9(1.5)}=\dfrac{0.128}{13.5}=9.5\times10^{-3}\ \text{m/s}$, about $1\ \text{cm/s}$.
(b) $F=6\pi\eta rv_t=6\pi(1.5)(1.0\times10^{-3})(9.50\times10^{-3})=2.7\times10^{-4}\ \text{N}$.
Balance $\tfrac43\pi r^3(\rho-\sigma)g=\tfrac43\pi(10^{-9})(6540)(9.8)=2.7\times10^{-4}\ \text{N}$ ✓.
Check The ball's weight alone is $3.2\times10^{-4}\ \text{N}$; the upthrust takes away about one-sixth of it. Interactive 2 starts from this ball.
Interactive 2 — Falling-Ball Viscometer

A ball is released at the top of a tall tube of liquid (slow falls are played back faster; the factor is shown under the tube, while the stopwatch keeps real time). The graph on the right is the ball's speed during its first moments, from Newton's second law with weight, upthrust and Stokes drag: the speed rises quickly and levels off at the terminal velocity $v_t$. Between the two marks $20\ \text{cm}$ apart the stopwatch times the fall, and the viscosity is worked back out from the measured speed. Try a larger ball, or a lighter one.

1.0 mm
terminal velocity $v_t$—
time to reach $0.99\,v_t$—
stopwatch (20 cm)—
$\eta$ worked back—
✏️ Example 4 — Measuring the viscosity of an oil
In a falling-ball viscometer, a steel ball of radius $2.0\ \text{mm}$ and density $7.8\times10^3\ \text{kg/m}^3$ falls through an oil of density $900\ \text{kg/m}^3$. After the first few centimetres it takes $5.0\ \text{s}$ to fall between two marks $30\ \text{cm}$ apart. Find the viscosity of the oil.
Speed $v_t=\dfrac{0.30}{5.0}=0.060\ \text{m/s}$ (constant, so it is the terminal velocity).
Viscosity $\eta=\dfrac{2r^2(\rho-\sigma)g}{9v_t}=\dfrac{2(2.0\times10^{-3})^2(6900)(9.8)}{9(0.060)}=\dfrac{0.541}{0.54}=1.0\ \text{Pa s}$ ($10$ poise).
Why "after the first few centimetres" The ball must have reached its terminal velocity before the timing starts; the marks are placed well below the surface (and away from the walls and bottom of the tube, which add extra drag).
Check An oil about as viscous as castor oil — plausible.
✏️ Example 5 — A rising bubble
An air bubble of radius $1.0\ \text{mm}$ rises through a syrup of density $1.4\times10^3\ \text{kg/m}^3$ and viscosity $2.0\ \text{Pa s}$. Find its terminal velocity, neglecting the density of the air.
Formula With $\rho\approx0$: $v_t=\dfrac{2r^2(0-\sigma)g}{9\eta}$, negative — the bubble moves up.
Numbers $|v_t|=\dfrac{2(1.0\times10^{-3})^2(1400)(9.8)}{9(2.0)}=\dfrac{0.02744}{18}=1.5\times10^{-3}\ \text{m/s}$, upward.
Forces Upthrust up, drag down (opposing the upward motion); the bubble's weight is negligible.
Check $1.5\ \text{mm/s}$ — that is why bubbles in thick syrup or shampoo take so long to rise and clear.
✏️ Example 6 — Drops that merge
Eight identical small raindrops, each falling with terminal velocity $5.0\ \text{cm/s}$ in Stokes' regime, coalesce into one drop. Find the terminal velocity of the big drop.
Radius The volume is conserved: $\tfrac43\pi R^3=8\times\tfrac43\pi r^3$, so $R=2r$.
Speed $v_t\propto r^2$ (same $\rho$, $\sigma$, $\eta$): $v=2^2\times5.0=20\ \text{cm/s}$.
General For $n$ drops, $R=n^{1/3}r$ and $v=n^{2/3}v_0$.
Check Not $8\times5.0$: the weight minus upthrust grows eight times, but the drag $6\pi\eta Rv$ is already doubled by the larger $R$, so $v$ need only grow four times: $8=2\times4$ ✓.
⚠️ Common mistakes

1. Forgetting the upthrust. At terminal velocity the drag equals weight minus upthrust, so $(\rho-\sigma)$ appears, not $\rho$ alone. In air the correction is tiny; in liquids it is not.

2. $r$ or $d$? Stokes' law uses the radius. Using the diameter makes $v_t$ four times too large.

3. $v_t\propto r$. The drag is proportional to $r$ but the weight to $r^3$, so $v_t\propto r^2$.

4. Using Stokes' law where it fails — for a falling cricket ball, a skydiver or a car the flow is turbulent and the drag is much larger.

5. Viscosity versus density. Oil is less dense than water but far more viscous. "Thick" in everyday speech means viscous.

6. Temperature. Liquids become less viscous when heated, gases more viscous.

🚀 Beyond the board syllabus (JEE Main · NEET · JEE Advanced) — how quickly is the terminal velocity reached?

In JEE Main, NEET and JEE Advanced (as part of Stokes' law and terminal velocity); not required by the CBSE syllabus.

For a sphere of mass $m=\tfrac43\pi r^3\rho$ released from rest, Newton's second law (ignoring the small mass of fluid dragged along) gives

$$m\frac{dv}{dt}=\tfrac43\pi r^3(\rho-\sigma)g-6\pi\eta rv=6\pi\eta r\,(v_t-v).$$

The acceleration is proportional to how far the speed is below $v_t$. The solution is

$$v(t)=v_t\left(1-e^{-t/\tau}\right),\qquad \tau=\frac{m}{6\pi\eta r}=\frac{2r^2\rho}{9\eta},$$

which you can check by differentiating ($\frac{d}{dt}e^{-t/\tau}=-\frac1\tau e^{-t/\tau}$, a rule you will meet in mathematics). After one time constant $\tau$ the speed is $63\%$ of $v_t$; after $5\tau$ it is within $1\%$. The initial acceleration is $g\left(1-\dfrac\sigma\rho\right)$. Example. For the steel ball of Example 3, $\tau=\dfrac{2(10^{-6})(7800)}{9(1.5)}=1.2\times10^{-3}\ \text{s}$: the ball reaches its terminal velocity within about $6\ \text{ms}$, after falling only about $0.05\ \text{mm}$. Interactive 2 draws this curve.

Exercises

Take $g=9.8\ \text{m/s}^2$, $\rho_\text{water}=1.00\times10^3\ \text{kg/m}^3$, $\eta_\text{water}=1.0\times10^{-3}\ \text{Pa s}$ and $\eta_\text{air}=1.8\times10^{-5}\ \text{Pa s}$; assume Stokes' law holds unless stated otherwise.

I
Viscosity.
  • 1 Find the dimensional formula and SI unit of the coefficient of viscosity. How many pascal seconds is one poise?
  • 2 A metal plate of area $0.20\ \text{m}^2$ slides at $0.050\ \text{m/s}$ over a $1.0\ \text{mm}$ layer of oil of viscosity $0.20\ \text{Pa s}$. Find the force needed.
  • 3 A force of $0.80\ \text{N}$ keeps a plate of area $0.040\ \text{m}^2$ moving at $2.0\ \text{cm/s}$ over a liquid film $0.30\ \text{mm}$ thick. Find the viscosity of the liquid.
  • 4 Honey flows more easily when warmed, but air becomes more viscous when heated. Explain both.
  • 5 Explain why, in laminar flow through a pipe, the liquid moves fastest along the axis.
  • 6 The top of a $2.0\ \text{mm}$ layer of glycerine ($\eta=1.5\ \text{Pa s}$) moves at $0.20\ \text{m/s}$ relative to the bottom. Find the velocity gradient and the shear stress.
  • 7 A $2.0\ \text{kg}$ block slides down a $30^\circ$ incline on an oil film $0.10\ \text{mm}$ thick ($\eta=0.15\ \text{Pa s}$); its area of contact is $0.050\ \text{m}^2$. Ignoring other friction, find the steady speed it reaches.
  • 8 Water ($\eta=1.0\times10^{-3}\ \text{Pa s}$, $\rho=1.0\times10^3\ \text{kg/m}^3$) flows at $5.0\ \text{cm/s}$ through a pipe $2.0\ \text{cm}$ in diameter. Find the Reynolds number, and the critical velocity above which the flow becomes turbulent (take $Re\approx2000$). Find the critical velocity for glycerine ($\eta=1.5\ \text{Pa s}$, $\rho=1.26\times10^3\ \text{kg/m}^3$) in the same pipe.
1 $\eta=\dfrac{F}{A(dv/dx)}$: $\dfrac{[\text{M L T}^{-2}]}{[\text{L}^2][\text{T}^{-1}]}=[\text{M L}^{-1}\text{T}^{-1}]$; unit $\text{N s/m}^2=\text{Pa s}$; $1\ \text{poise}=0.1\ \text{Pa s}$.
2 $F=\eta A\dfrac vl=0.20\times0.20\times\dfrac{0.050}{1.0\times10^{-3}}=2.0\ \text{N}$.
3 $\eta=\dfrac{Fl}{Av}=\dfrac{0.80\times3.0\times10^{-4}}{0.040\times0.020}=0.30\ \text{Pa s}$.
4 In a liquid, viscosity comes from the attraction between neighbouring molecules; warmer molecules break free more easily, so layers slide more easily. In a gas, molecules crossing between layers carry momentum and drag the layers together; hotter molecules cross faster and more often, increasing the drag.
5 The liquid at the wall sticks to it ($v=0$); each layer is dragged back by the slower layer outside it, so speed builds up towards the axis, where it is greatest.
6 $\dfrac{dv}{dx}=\dfrac{0.20}{2.0\times10^{-3}}=100\ \text{s}^{-1}$; stress $=1.5\times100=150\ \text{Pa}$.
7 Steady when $mg\sin30^\circ=\eta A\dfrac vl$: $v=\dfrac{2.0(9.8)(0.50)(1.0\times10^{-4})}{0.15\times0.050}=0.13\ \text{m/s}$.
8 $Re=\dfrac{1.0\times10^3\times0.050\times0.020}{1.0\times10^{-3}}=1.0\times10^3$ — laminar. $v_c\approx\dfrac{2000\times1.0\times10^{-3}}{1.0\times10^3\times0.020}=0.10\ \text{m/s}$. Glycerine: $v_c\approx\dfrac{2000\times1.5}{1.26\times10^3\times0.020}=1.2\times10^2\ \text{m/s}$ — its flow in such a pipe is laminar at any practical speed.
II
Stokes' law and terminal velocity.
  • 1 Find the drag on a sphere of radius $0.50\ \text{mm}$ moving at $2.0\ \text{cm/s}$ through glycerine ($\eta=1.5\ \text{Pa s}$).
  • 2 Assuming the drag on a slowly moving sphere depends only on $\eta$, $r$ and $v$, use dimensional analysis to show that $F\propto\eta rv$.
  • 3 Find the terminal velocity of an oil droplet of radius $2.0\ \mu\text{m}$ and density $900\ \text{kg/m}^3$ falling through air (neglect the upthrust of the air).
  • 4 A steel ball of radius $1.5\ \text{mm}$ (density $7.8\times10^3\ \text{kg/m}^3$) falls through castor oil (density $960\ \text{kg/m}^3$, $\eta=0.99\ \text{Pa s}$). Find its terminal velocity.
  • 5 Two spheres of the same material, of radii in the ratio $1:3$, fall through the same liquid. Find the ratio of their terminal velocities.
  • 6 Twenty-seven identical droplets, each with terminal velocity $2.0\ \text{mm/s}$, merge into one drop. Find its terminal velocity.
  • 7 A ball falls at its terminal velocity. What are the net force on it and its acceleration? What happens to the gravitational potential energy it loses?
  • 8 An air bubble of radius $0.50\ \text{mm}$ rises through a liquid of density $1.2\times10^3\ \text{kg/m}^3$ and viscosity $0.60\ \text{Pa s}$. Find its terminal velocity.
1 $F=6\pi(1.5)(5.0\times10^{-4})(0.020)=2.8\times10^{-4}\ \text{N}$.
2 $F=k\eta^ar^bv^c$: $[\text{M L T}^{-2}]=[\text{M}]^a[\text{L}]^{-a+b+c}[\text{T}]^{-a-c}$, so $a=1$, $c=1$, $b=1$: $F=k\eta rv$.
3 $v_t=\dfrac{2(2.0\times10^{-6})^2(900)(9.8)}{9(1.8\times10^{-5})}=4.4\times10^{-4}\ \text{m/s}$ ($0.44\ \text{mm/s}$).
4 $v_t=\dfrac{2(1.5\times10^{-3})^2(6840)(9.8)}{9(0.99)}=3.4\times10^{-2}\ \text{m/s}$.
5 $v_t\propto r^2$: $1:9$.
6 $R=27^{1/3}r=3r$, so $v=9\times2.0=18\ \text{mm/s}$.
7 Net force zero, acceleration zero. The kinetic energy is constant, so the potential energy lost (less the work against the upthrust) is turned into heat in the liquid by the viscous force.
8 $|v_t|=\dfrac{2(5.0\times10^{-4})^2(1200)(9.8)}{9(0.60)}=1.1\times10^{-3}\ \text{m/s}$, upward.
III
Applications.
  • 1 (Modelling) In a falling-ball viscometer a steel ball of radius $1.0\ \text{mm}$ (density $7.8\times10^3\ \text{kg/m}^3$) falls $20\ \text{cm}$ in $25\ \text{s}$ at constant speed through a liquid of density $1.26\times10^3\ \text{kg/m}^3$. Find the viscosity of the liquid.
  • 2 (Modelling) Sand grains of radius $0.050\ \text{mm}$ (density $2650\ \text{kg/m}^3$) settle in still water. Find their terminal velocity and the time to settle through $2.0\ \text{m}$. How long would clay particles of radius $1.0\ \mu\text{m}$ of the same density take?
  • 3 Fog consists of water droplets of radius about $5.0\ \mu\text{m}$. Find their terminal velocity in air and explain why fog seems to hang in the air.
  • 4 In a centrifuge, particles in a test tube behave as if $g$ were replaced by a much larger acceleration. Explain why blood cells separate from plasma much faster in a centrifuge than when left to stand.
  • 5 A skydiver also reaches a terminal speed, of about $55\ \text{m/s}$. Explain why, and why Stokes' law cannot be used to calculate it.
  • 6 Find the power needed to keep the plate of Exercise I.2 moving, and say where the energy goes.
1 $v_t=\dfrac{0.20}{25}=8.0\times10^{-3}\ \text{m/s}$; $\eta=\dfrac{2(1.0\times10^{-3})^2(6540)(9.8)}{9(8.0\times10^{-3})}=1.8\ \text{Pa s}$.
2 $v_t=\dfrac{2(5.0\times10^{-5})^2(1650)(9.8)}{9(1.0\times10^{-3})}=9.0\times10^{-3}\ \text{m/s}$; $t=\dfrac{2.0}{0.0090}=2.2\times10^2\ \text{s}$, under four minutes. Clay: $r$ is $50$ times smaller, so $v_t$ is $2500$ times smaller ($3.6\times10^{-6}\ \text{m/s}$) and $t=5.6\times10^5\ \text{s}$, about $6$ days — why muddy water stays cloudy.
3 $v_t=\dfrac{2(5.0\times10^{-6})^2(1000)(9.8)}{9(1.8\times10^{-5})}=3.0\times10^{-3}\ \text{m/s}$, $3\ \text{mm/s}$ — less than the slowest air currents, which keep the droplets suspended.
4 $v_t=\dfrac{2r^2(\rho-\sigma)a}{9\eta}$ with $a$ the centrifuge's effective acceleration, thousands of times $g$; the cells (slightly denser than plasma) drift down thousands of times faster.
5 As the skydiver speeds up, air resistance grows until it equals the weight; then the net force and acceleration are zero. The body is large and fast, so the air flow round it is turbulent and the drag grows roughly as $v^2$, not as $6\pi\eta rv$.
6 $P=Fv=2.0\times0.050=0.10\ \text{W}$, dissipated as heat in the oil.
IV
Harder problems.
  • 1 A sphere falling at its terminal velocity experiences a viscous force $F$. Find the viscous force on a sphere of the same material with twice the radius, also at its terminal velocity, in the same liquid.
  • 2 A steel ball and an aluminium ball of the same radius fall through glycerine. Find the ratio of their terminal velocities (densities $7800$, $2700$ and $1260\ \text{kg/m}^3$).
  • 3 Check that the formula $v_t=\dfrac{2r^2(\rho-\sigma)g}{9\eta}$ is dimensionally correct.
  • 4 Two spheres of the same radius, of densities $2000$ and $1000\ \text{kg/m}^3$, are released in a liquid of density $1500\ \text{kg/m}^3$. Compare their terminal velocities.
  • 5 At what rate is heat produced in the glycerine by the steel ball of Example 3 once it is at its terminal velocity?
1 At terminal velocity the drag equals $\tfrac43\pi r^3(\rho-\sigma)g\propto r^3$: $8F$. (Equivalently $6\pi\eta rv_t$ with $v_t\propto r^2$.)
2 $\dfrac{7800-1260}{2700-1260}=\dfrac{6540}{1440}=4.5$.
3 $\dfrac{[\text{L}^2][\text{M L}^{-3}][\text{L T}^{-2}]}{[\text{M L}^{-1}\text{T}^{-1}]}=\dfrac{[\text{M L}^{0}\text{T}^{-2}]}{[\text{M L}^{-1}\text{T}^{-1}]}=[\text{L T}^{-1}]$ ✓.
4 $\rho-\sigma=+500$ and $-500\ \text{kg/m}^3$: equal speeds, the first sinking and the second rising.
5 $P=Fv_t=2.68\times10^{-4}\times9.50\times10^{-3}=2.5\times10^{-6}\ \text{W}$.
🎯 Exam corner BoardJEE MainJEE AdvancedNEET

E1. Board · 2 marks Define the coefficient of viscosity. Write its SI unit and dimensional formula.

Definition The tangential viscous force per unit area between two layers of a fluid in laminar flow, per unit velocity gradient: $\eta=\dfrac{F/A}{dv/dx}$. [1]
Units $\text{Pa s}$ ($\text{N s m}^{-2}$); $[\text{M L}^{-1}\text{T}^{-1}]$. [1]
Exam tip Say "laminar flow" and "velocity gradient perpendicular to the flow" — both are needed for full marks.

E2. NEET Two identical raindrops fall through air with terminal velocity $5.0\ \text{cm/s}$. They merge into a single drop. Its terminal velocity is (a) $10\ \text{cm/s}$ (b) $5.0\times2^{2/3}\ \text{cm/s}$ (c) $5.0\times2^{1/3}\ \text{cm/s}$ (d) $2.5\ \text{cm/s}$

Idea Volume doubles: $R=2^{1/3}r$. $v_t\propto r^2$, so $v=2^{2/3}\times5.0\approx7.9\ \text{cm/s}$.
Answer (b).
Exam tip (a) assumes the radius doubles; (c) uses $v_t\propto r$.

E3. JEE Main (Numerical value) A steel ball of radius $2.0\ \text{mm}$ and density $8.0\times10^3\ \text{kg/m}^3$ falls through a liquid of density $1.0\times10^3\ \text{kg/m}^3$ with a terminal velocity of $4.0\ \text{cm/s}$. Find the viscosity of the liquid in Pa s, to two decimal places. (Take $g=9.8\ \text{m/s}^2$.)

Set-up $\eta=\dfrac{2r^2(\rho-\sigma)g}{9v_t}=\dfrac{2(2.0\times10^{-3})^2(7000)(9.8)}{9(0.040)}$.
Answer $\dfrac{0.5488}{0.36}=1.52\ \text{Pa s}$ ($15.2$ poise).
Exam tip Using the diameter gives $6.10$; forgetting the upthrust gives $1.74$ — both appear as distractors.

E4. JEE Advanced (One or more correct) A small sphere of density $\rho$ is released from rest in a large tank of liquid of density $\sigma\lt\rho$ and viscosity $\eta$, and Stokes' law holds. Neglecting the mass of liquid carried along, which statements are correct? (A) Its initial acceleration is $g\left(1-\dfrac{\sigma}{\rho}\right)$. (B) Its acceleration decreases steadily to zero. (C) Its terminal velocity is proportional to the square of its radius. (D) At terminal velocity the viscous force equals the weight of the sphere.

(A) At $v=0$ there is no drag: $ma=\tfrac43\pi r^3(\rho-\sigma)g$ with $m=\tfrac43\pi r^3\rho$, so $a=g(1-\sigma/\rho)$ ✓.
(B) As $v$ grows the drag grows and the net force falls; $a\to0$ as $v\to v_t$ ✓ (exponentially, in fact).
(C) $v_t=\dfrac{2r^2(\rho-\sigma)g}{9\eta}\propto r^2$ ✓.
(D) The viscous force equals the weight minus the upthrust ✗.
Answer (A), (B), (C).
Exam tip Limiting check on (A): if $\sigma=\rho$ the sphere would not move at all, and indeed $a=0$.

E5. JEE Main NEET A small sphere falling through a viscous liquid at its terminal velocity experiences a viscous force $F$. A sphere of the same material and twice the radius, also at its terminal velocity in the same liquid, experiences a viscous force (a) $2F$ (b) $4F$ (c) $8F$ (d) $16F$

Idea $F=6\pi\eta rv_t$ with $v_t\propto r^2$, so $F\propto r^3$ — it must balance the weight minus upthrust, which is proportional to the volume.
Answer $2^3F=8F$: (c).
Exam tip (a) treats $v$ as fixed; (b) treats $F\propto r^2$ like the terminal speed.

E6. Board · Case study In a school laboratory a steel ball of radius $1.5\ \text{mm}$ (density $7.8\times10^3\ \text{kg/m}^3$) is dropped into a tall jar of glycerine (density $1.26\times10^3\ \text{kg/m}^3$). Two rubber bands, $10.0\ \text{cm}$ apart, are placed well below the surface; the ball takes $6.0\ \text{s}$ to pass from one to the other. (i) Explain why the ball soon falls at a constant speed. [1] (ii) Find the viscosity of the glycerine. [2] (iii) Why are the bands placed well below the surface? [1]

(i) The viscous drag $6\pi\eta rv$ grows with speed until it balances the weight minus the upthrust; the net force is then zero, so the speed stays constant (terminal velocity). [1]
(ii) $v_t=\dfrac{0.100}{6.0}=0.0167\ \text{m/s}$. $\eta=\dfrac{2(1.5\times10^{-3})^2(6540)(9.8)}{9(0.0167)}=1.9\ \text{Pa s}$. [2]
(iii) So that the ball has already reached its terminal velocity before timing starts; the formula holds only at constant speed. [1]
Exam tip The value is a little above the $1.5\ \text{Pa s}$ quoted at $20\ ^\circ\text{C}$ — glycerine is very sensitive to temperature, and the walls of a narrow jar add extra drag.
🔬 Research–Teaching NexusResearch-tutored · optional, about 40 minutes

Research question. Why does fine air pollution (PM2.5) linger over a city for days, while coarse dust settles within hours?

Why it matters. The World Health Organization links fine particulate matter to millions of early deaths a year. Particles are classed by size: PM10 (diameter up to $10\ \mu\text{m}$) and PM2.5 (up to $2.5\ \mu\text{m}$). In winter smog in Delhi, Beijing or Lahore, the air is often still and a temperature inversion acts as a lid about a kilometre up — so how long the particles take to settle matters for public health.

What to do. Treat particles as spheres of density $1.5\times10^3\ \text{kg/m}^3$ falling through still air ($\eta=1.8\times10^{-5}\ \text{Pa s}$), where Stokes' law is an excellent approximation.

  1. Find the terminal velocity of a PM2.5 particle (diameter $2.5\ \mu\text{m}$) and of a PM10 particle (diameter $10\ \mu\text{m}$).
  2. How long would each take to fall $1.0\ \text{km}$ in perfectly still air? Express your answers in days.
  3. Sand-sized dust has a diameter of about $100\ \mu\text{m}$. Show that Stokes' law predicts a speed of about $0.5\ \text{m/s}$. Why should you distrust it at that size?
  4. Rain removes particles much faster than settling. Suggest why.
  5. Use your numbers to explain to a city council why PM2.5 is more dangerous than PM10 over a long smog episode.

Tools: Calculator or spreadsheet; air-quality data for your own city from a public monitoring website; optionally a jar of muddy water to watch coarse and fine particles settle at different rates.

Hand in: A table of particle size, terminal velocity and settling time; a log–log graph of $v_t$ against diameter; and a one-page briefing note for a city council.

Going further. For particles smaller than about $1\ \mu\text{m}$ the air no longer behaves like a continuous fluid around them. Find out what the "Cunningham slip correction" does to the settling speed.

Instructor note: PM2.5 ($r=1.25\ \mu\text{m}$): $v_t=\dfrac{2r^2\rho g}{9\eta}=2.8\times10^{-4}\ \text{m/s}$, so $1\ \text{km}$ takes $3.5\times10^6\ \text{s}\approx41$ days. PM10 ($r=5\ \mu\text{m}$): $16$ times faster, $4.5\times10^{-3}\ \text{m/s}$, about $2.6$ days. $100\ \mu\text{m}$: $0.45\ \text{m/s}$; the flow round it is no longer fully laminar, so the true speed is somewhat lower. In practice turbulence and winds mix particles, and rain (drops sweeping up particles) or deposition on surfaces remove them — settling alone is far too slow for fine particles.

🧪 Self-check quiz

0/5 correct

Q1. The SI unit of the coefficient of viscosity is

Q2. When a liquid is heated, its viscosity

Q3. In Stokes' regime the terminal velocity of a small sphere falling through a liquid is proportional to

Q4. A ball is falling through oil at its terminal velocity. The net force on the ball is

Q5. According to Stokes' law, if a small sphere moves through a fluid twice as fast, the viscous drag on it