The authors of this paper are commended for the very clear and workman-like presentation of their case. The list of references indicates an exceptionally thorough job of researching the topic.While in recent times, with the advent of the high-speed digital computer, there has been a tendency toward the solution of the boundary layer equations as opposed to momentum integral forms, the potential use and importance of momentum integral solutions should not be underestimated. Many, if not most, of the quick and more useful engineering type approximate calculations for two-dimensional turbulent boundary layers 3 are based on momentum integral forms, and with the three-dimensional problem being even more complicated one might reasonably expect some of the engineering type relationships which would prove useful in real-wo rid design to come from such solutions.The cross flow velocity profile model presented is unusually flexible and potentially very useful in that it covers a very broad range of possible flows as demonstrated by its ability to predict, with reaonably good agreement, some of the heretofore unyielding internal flows with 3dtbls, and this is highly encouraging.The need for such an all-encompassing model is clear, but a few remarks will be directed toward the authors' conditions iii and iv, and some concern is expressed on possible problems in the closure of the mathematical problem in an unknown flow field. The question of a collateral near-wall region of flow in threedimensional turbulent layers is still open. The work of Francis and Pierce [36], 4 Klinksiek and Pierce [37], Gardow [38], Johnston [39], Hornung and Joubert [40], M. Smith [41], P. D. Smith [42], Lewkowicz [43], and Prahlad [44], all show from two up to seven experimentally determined points which suggest a collateral near-wall region of flow when w/U is plotted against u/U in a velocity polar (or hodograph) figure. In all cases the velocity polars referred to above were characterized by lateral flow in only one direction so that these polars can be put into a single class of flows.While the polar is very useful in demonstrating the nature of the transverse flow, it is lacking in that the physical distance from the wall is totally absent and one must be careful to note that the right half of a typical polar represents some 80 to 90 percent of the boundary layer thickness while the left half represents only 10 or 20 percent. As a result, the data points which infer a collateral near-wall region are usually taken over a very small physical distance. East [45] show some interesting results. East used an explicit DuFort Frankel approach to solve the full 3dtbl equations for the impinging jet flow studied experimentally by Johnston. The particular flow studied was chosen in that the thorough documentation by Johnston provided a means of evaluation of the success of the finite difference solution. The solution utilized a mixing length hypothesis relating the turbulent stresses to the mean velocity gradients after the generalized treatment attrib...