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, $\dfrac{v}{l}$.
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 $[\text{M L}^{-1}\text{T}^{-1}]$.
| Fluid | Temperature | $\eta$ (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.
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 $k=6\pi$.
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.
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:
$$6\pi\eta rv_t=\tfrac43\pi r^3(\rho-\sigma)g .$$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 $\eta=\dfrac{2r^2(\rho-\sigma)g}{9v_t}$.
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.
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.
- 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 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 (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 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?
E1. Board · 2 marks Define the coefficient of viscosity. Write its SI unit and dimensional formula.
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) $2.5\ \text{cm/s}$
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 $g=9.8\ \text{m/s}^2$.)
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.
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) $16F$
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]
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.
- Find the terminal velocity of a PM2.5 particle (diameter $2.5\ \mu\text{m}$) and of a PM10 particle (diameter $10\ \mu\text{m}$).
- How long would each take to fall $1.0\ \text{km}$ in perfectly still air? Express your answers in days.
- 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?
- Rain removes particles much faster than settling. Suggest why.
- 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.
🧪 Self-check quiz
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