 Solution

A velocity field $\mathbf{u}(\mathbf{x},t)$ assigns a velocity to each point. Following a fluid parcel rather than holding position fixed gives the material or convective derivativeThe convective term can accelerate fluid even in a steady flow, for example as a stream narrows. Conservation of mass is ${\partial }_t\rho +\nabla \cdot (\rho \mathbf{u})=0$; constant-density incompressible flow has $\nabla \cdot \mathbf{u}=0$.

For an incompressible Newtonian fluid of constant density and viscosity, with conservative body-force potential per mass $\Phi$, momentum balance isNeglect viscosity and assume steady flow. Dotting with an element along a streamline, or using $(\mathbf{u}\cdot \nabla )\mathbf{u}=\nabla (u^2/2)-\mathbf{u}\times (\nabla \times \mathbf{u})$, givesThis is Bernoulli's equation: pressure work, kinetic energy and gravitational potential energy interconvert. In a connected irrotational region under the same assumptions, $B$ is the same for all streamlines. In a rotational flow it can vary between them. Viscous dissipation, pumps or unsteady motion require the corresponding modified balance; the steady inviscid expression cannot be applied indiscriminately.

Vorticity $\mathbf{\zeta }=\nabla \times \mathbf{u}$ measures local fluid rotation. For constant-density incompressible flow it evolves byshowing vortex stretching and viscous diffusion. A potential flow has $\mathbf{u}=\nabla \varphi$ locally, so irrotational incompressible motion satisfies ${\nabla }^2\varphi =0$. Boundary conditions then determine flows around simple shapes. A multiply connected region can have circulation even when its local vorticity vanishes; ideal potential flow also misses no-slip boundary layers and viscous drag.

For a Newtonian fluid, shear stress is proportional to strain rate. No-slip at solid walls produces velocity gradients and dissipation. Fully developed laminar pipe flow, for example, hasThe Reynolds number $\mathrm{Re}=UL/\nu$ compares inertial and viscous terms. Small values favour creeping-flow approximations; large values can permit thin boundary layers and turbulence, without guaranteeing turbulence in every geometry. The appropriate flow model follows from conservation laws, constitutive properties, boundaries and scale comparisons.