The wall speed sets
Using as the local streamwise length gives
which is large when . The boundary-layer scaling
then gives
so the stretching-sheet layer has constant thickness to leading order.
With zero imposed pressure gradient, the two-dimensional boundary-layer equations are
Introduce the stream function by
The boundary conditions are
The additive constant in may be chosen so that .
Put
Then
Substitution in the boundary-layer momentum equation, using , gives
The wall and far-field conditions become
These are the similarity equations for the boundary layer over a linearly stretching sheet.
Set with . The differential equation reduces to
so . The two wall conditions give
Hence , and positivity of yields
or
As ,
Thus the tangential velocity matches the quiescent outer fluid, but the normal velocity tends to
The stretching sheet entrains fluid toward itself at a constant leading-order speed. Consequently a globally stationary exterior flow is impossible: the outer flow must provide this normal influx and complete the mass balance away from the local boundary-layer approximation.

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