Dynamic Viscosity Explained: Formula & No-Slip Condition

The property that resists a fluid's rate of deformation — and why the fluid at the wall always matches the wall.

Foundations: Fluid PropertiesMechanical EngineeringFree preview
⏱️ About 18 min

Tilt a jar of honey and a jar of water the same way. The water rushes out in a splash; the honey crawls, taking its time to slump toward the opening. Both feel the same gravity, both have similar densities, yet one barely moves. The difference is not weight — it is <em>viscosity</em>, the internal friction that resists how fast a fluid deforms. And here is a trap that catches almost every beginner: viscosity and density are entirely different properties. Honey is viscous but not especially dense; mercury is staggeringly dense but pours almost as freely as water. 'Thick' and 'heavy' are not the same word, and confusing them derails half the reasoning in pipe flow. This lesson separates them cleanly and introduces the no-slip condition, the rule that glues a fluid to whatever wall touches it.

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The big idea: Newton's law of viscosity says the shear stress in a fluid is proportional to the velocity gradient: τ = μ (du/dy). The constant of proportionality, μ, is the <strong>dynamic viscosity</strong> — a fluid's resistance to rate of deformation. For a class of fluids called <strong>Newtonian</strong> (water, air, most oils and gases), μ depends only on temperature and pressure, not on how hard you stir; <strong>non-Newtonian</strong> fluids (paint, blood, ketchup) change their viscosity with the shear rate itself. Two further facts: viscosity depends strongly on temperature (liquids thin out as they heat, gases thicken), and the <strong>no-slip condition</strong> forces the fluid in contact with a solid wall to move at the wall's velocity — regardless of how smooth that wall is.
🎯 By the end, you'll be able to
  • State Newton's law of viscosity and use τ = μ du/dy to compute shear stress
  • Distinguish dynamic viscosity μ from kinematic viscosity ν = μ/ρ
  • Explain how viscosity depends on temperature for liquids and for gases
  • Contrast Newtonian and non-Newtonian fluids with examples
  • State the no-slip condition and explain why wall smoothness does not change it
📎 Helpful to know first

Newton's law of viscosity

Picture fluid trapped between two parallel plates a small distance h apart. Hold the bottom plate fixed and drag the top plate sideways at speed U. What happens? The fluid does not slide under the plate as a rigid block; instead it shears into layers, each dragging the one beneath it. Experiments show the velocity rises linearly from zero at the fixed plate to U at the moving plate, so the velocity gradient du/dy = U/h is constant. The shear stress needed to hold the top plate moving turns out to be proportional to exactly that gradient. The constant of proportionality is the dynamic viscosity.

\[ \tau = \mu\,\frac{du}{dy} \]
Newton's law of viscosity for a Newtonian fluid. The shear stress τ is proportional to the velocity gradient (shear rate) du/dy; the constant μ is the dynamic viscosity (units Pa·s = N·s/m²). For the linear profile between moving plates, du/dy = U/h and τ = μU/h is uniform across the gap.
Plane Couette flow: a top plate moving at speed U drags the fluid between it and a fixed bottom plate into a straight, linear velocity profile u = U y/h, rising from zero at the bottom plate to U at the top. The velocity gradient du/dy is constant, giving a uniform shear stress tau = mu du/dy. U (plate speed) h du/dy = U/h u = U u = 0 τ = μ du/dy (uniform) flow A linear profile means a constant gradient du/dy, so Newton's law gives a shear stress τ that is the same at every height.

A top plate moving at speed U over a fixed bottom plate, with fluid between them. The velocity profile is a straight line rising from zero at the bottom plate to U at the top plate. The gap height h is marked, the constant gradient du/dy = U/h is labelled, and the uniform shear stress tau = mu du/dy is noted.

Plane Couette flow: a moving plate drags the fluid into a linear profile. Because du/dy = U/h is constant, Newton's law gives a shear stress τ = μU/h that is the same at every height — every layer drags its neighbour with equal force.
⚠️ Viscosity is NOT density

This is the misconception this lesson exists to kill. People say a fluid is 'thick' when they mean viscous, and 'heavy' when they mean dense — and then they assume the two go together. They do not. Honey is roughly 10 000 times more viscous than water (μ ≈ 10 Pa·s versus 1.0 × 10⁻³ Pa·s), yet its density (≈ 1400 kg/m³) is barely above water's. Mercury is 13.6 times denser than water (ρ ≈ 13 600 kg/m³) but has about the same viscosity as water (μ ≈ 1.5 × 10⁻³ Pa·s) — it pours freely despite being enormously heavy. Viscosity measures resistance to rate of deformation; density measures mass per volume. They are independent properties. Never reason from one to the other.

Dynamic versus kinematic viscosity

Engineers carry two forms of viscosity. Dynamic viscosity μ (Pa·s) appears directly in Newton's law, τ = μ du/dy — it is the genuine material property. Kinematic viscosity ν = μ/ρ (m²/s) is dynamic viscosity divided by density, and it shows up whenever inertia matters, as in the Reynolds number Re = VD/ν. The two have different units and different physical meanings, so keep them straight: μ answers 'how hard does this fluid resist shearing?', while ν answers 'how readily does momentum diffuse through this fluid?'. Oil has high μ but, being dense, only moderate ν; the distinction matters the moment you compute a Reynolds number.

\[ \nu = \frac{\mu}{\rho} \qquad [\nu] = \text{m}^{2}/\text{s} \]
Kinematic viscosity ν is dynamic viscosity divided by density. Its units (m²/s) reveal its character: it is a diffusivity — the rate at which momentum (and velocity disturbances) spread through the fluid. The older unit, the centistokes (1 cSt = 1 mm²/s = 10⁻⁶ m²/s), is still common in the oil industry.

Temperature dependence: why oil thins when hot

Viscosity depends strongly on temperature, and — surprisingly — the direction is opposite for liquids and gases. In a liquid, viscosity comes from molecules clinging to one another; heating gives them energy to break those bonds, so a liquid's viscosity falls sharply as it warms. Motor oil is noticeably thinner at operating temperature than on a cold morning, which is exactly why multi-grade oils are engineered to behave well across a wide temperature range. In a gas, by contrast, viscosity comes from molecules colliding and exchanging momentum; heating makes them move faster and collide more often, so a gas's viscosity rises with temperature. Hot air is marginally more viscous than cold air — the reverse of the liquid trend. Pressure has only a weak effect on viscosity for liquids and gases at ordinary conditions.

✨ Newtonian versus non-Newtonian fluids

Newton's law τ = μ du/dy assumes μ is a constant at a given temperature and pressure, independent of how fast you shear the fluid. Fluids that obey this are Newtonian: water, air, gasoline, and most common oils and gases. Their shear stress plots as a straight line through the origin versus shear rate, with slope μ.

Many real fluids do not. Non-Newtonian fluids have an effective viscosity that changes with the shear rate itself: shear-thinning fluids (paint, blood, ketchup) get thinner the harder you stir — that is why paint spreads smoothly under the brush but does not drip off the wall; shear-thickening fluids (a cornstarch-and-water slurry) stiffen when you hit them, so you can walk slowly across a pool of it but punch through if you stand still; Bingham plastics (toothpaste, mayonnaise) behave as a solid until the stress exceeds a yield point, then flow. For most of this course we treat fluids as Newtonian, but you should know the category exists.

The no-slip condition

There is one boundary rule that holds for every viscous fluid against every solid wall, and it underlies nearly every result in this course: the no-slip condition. It says that the fluid in immediate contact with a solid boundary moves at exactly the velocity of that boundary. A wall at rest holds the fluid next to it at rest; a moving wall drags the adjacent fluid along with it at the wall's speed. There is no sliding, no gap, no slip — the fluid is effectively glued to the surface.

Why does this hold? At the microscopic scale, fluid molecules constantly collide with the far heavier, slower wall molecules and, on average, take up the wall's velocity; and any fluid that might try to slide is held back by the viscous transmission of that drag through the layers above. The crucial point is that no-slip is independent of how smooth the wall is. A hand-polished glass tube and a rough cast-iron pipe both enforce no-slip equally — the fluid at the wall is at rest in both. Wall roughness changes turbulent friction later, but it does not weaken the no-slip condition, which is set by molecular contact, not by surface texture.

🔑 No-slip is why walls have friction — and why profiles curve

The no-slip condition is the seed of all viscous friction. Because the fluid at a stationary wall is stuck at zero, yet the bulk fluid far from the wall moves freely, there must be a velocity gradient near the wall — and by Newton's law that gradient is exactly a shear stress on the wall. No no-slip, no wall shear, no pipe friction. It is also what forces a flowing fluid's velocity profile to be curved (parabolic in laminar pipe flow, flatter in turbulent flow) rather than a uniform block: the walls pin the edges to zero while inertia carries the centre along. When you meet the parabolic profile and the Moody chart in later modules, remember that both grow from this single rule.

🎮 Interactive: Newton's law of viscosity LIVE
Predict first: Honey (μ ≈ 10 Pa·s) versus water (μ ≈ 0.001 Pa·s) for the same plate speed and gap. How many times larger is the shear stress in honey?

An interactive slider tool computing the shear stress between parallel plates from dynamic viscosity, plate speed, and gap height, using Newton's law of viscosity.

Compute the wall shear stress τ = μU/h live as you vary viscosity, plate speed, and gap. Viscosity spans water to honey; note how shear stress scales linearly with μ, U, and inversely with h.
📝 Worked example: Glycerin (μ = 1.5 Pa·s) fills the gap h = 1.0 mm = 0.001 m between two plates. The top plate moves at U = 0.3 m/s and the bottom plate is fixed (plane Couette flow). Find the shear stress and state the velocity profile.
  1. For plane Couette flow the profile is linear, u = Uy/h, with constant gradient du/dy = U/h.
  2. Newton's law: τ = μ du/dy = μU/h = (1.5)(0.3)/(0.001).
  3. μU = 1.5 × 0.3 = 0.45; τ = 0.45/0.001 = 450 Pa.
  4. Profile: u = (0.3/0.001) y = 300 y (m/s, y in metres), rising linearly from 0 to 0.3 m/s across the gap.
  5. Units check: (Pa·s)(m/s)/m = Pa. ✓
✓ τ = 450 Pa, uniform across the gap; profile u = 300 y (linear).
✏️ Practice: An oil with μ = 0.08 Pa·s fills a gap h = 0.5 mm = 0.0005 m between plates. The top plate moves at U = 0.4 m/s, the bottom fixed. Find the shear stress τ, in Pa.
Pa
Solution
  1. τ = μU/h = (0.08)(0.4)/(0.0005) = 0.032/0.0005 = 64 Pa.
✏️ Practice: An oil has dynamic viscosity μ = 0.04 Pa·s and density ρ = 900 kg/m³. Find its kinematic viscosity ν, giving the answer in units of 10⁻⁵ m²/s.
×10⁻⁵ m²/s
Solution
  1. ν = μ/ρ = 0.04/900 = 4.44 × 10⁻⁵ m²/s.
  2. In the requested units of 10⁻⁵ m²/s, that is 4.44.

Check your understanding

1. Viscosity (dynamic viscosity μ) is best described as a fluid's:
μ is the proportionality constant between shear stress and shear rate. It measures how hard a fluid resists being deformed quickly. Density measures mass per volume — a separate, independent property (honey is viscous but not dense; mercury is dense but not viscous).
2. The no-slip condition states that:
No-slip means the fluid right at a wall shares the wall's velocity — zero at a fixed wall, U at a moving one. It is set by molecular contact and holds equally for polished glass and rough iron; surface texture does not weaken it.
3. How does viscosity typically change with temperature?
Liquids thin out as they heat (intermolecular bonds weaken), so μ falls — motor oil is thinner hot than cold. Gases thicken as they heat (faster molecules collide and transfer momentum more often), so μ rises. The trends are opposite.
✅ Key takeaways
  • Newton's law of viscosity: τ = μ du/dy. Dynamic viscosity μ (Pa·s) is a fluid's resistance to the rate of shear deformation.
  • Viscosity is not density — honey is viscous but only mildly dense; mercury is dense but flows almost like water.
  • Kinematic viscosity ν = μ/ρ (m²/s) is a momentum diffusivity; it appears in the Reynolds number Re = VD/ν.
  • Liquids thin as they heat (μ falls); gases thicken as they heat (μ rises). Newtonian fluids have constant μ at a given T, P; non-Newtonian fluids do not.
  • The no-slip condition pins the fluid at a wall to the wall's velocity, regardless of wall smoothness — it is the origin of all viscous wall friction.
➡️ Viscosity and the no-slip condition describe how a fluid resists deformation and clings to walls. But another question is still open: how much does a fluid resist being squeezed — compressed? For gases the answer is 'a great deal', and for liquids 'almost not at all'. That property, the bulk modulus, is what lets us treat water as incompressible in nearly every flow we will study — and it sets up why compressible flow is an entirely separate subject.
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