The following restrictions exist for the macro heat exchanger models:
The core must be approximately rectangular in shape.
The primary fluid streamwise direction (see
this equation in the separate
Theory Guide) must be aligned with one of the three orthogonal axes defined by the rectangular core.
Flow acceleration effects are neglected in calculating the pressure loss coefficient.
For the
simple-effectiveness-model, the primary fluid capacity rate must be less than the auxiliary fluid capacity rate.
Auxiliary fluid phase change cannot be modeled using the
ntu-model.
The macro-based method requires that an equal number of cells reside in each macro of equal size and shape.
Coolant flow is assumed to be 1-D.
The pass width has to be uniform.
Accuracy is not guaranteed when the mesh is not structured or layered.
Accuracy is not guaranteed when there is upstream diffusion of temperature at the inlet/outlet of the core.
Non-conformal meshes cannot be attached to the inlet/outlet of the core. An extra layer has to be created to avoid it.