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The location of the maximum mass flux divergence determines the failure location in the static case.
For the latter, maximum mass flux is desired because a freer exhaust is preferable.
This model is subsequently used to optimise both operating and design parameters for maximum mass flux in hollow fibre liquid membranes.
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Here, increased flame temperatures lead to a dramatic increase of the maximum supportable mass flux.
This effect, combined with the step function used for the approximation of Q t), justifies the definition Q tot_max as the maximum theoretical mass flux.
According to Fig. 13, the maximum asphaltene mass flux in the flow path from the reservoir to the surface is deposited in a depth of 12,000 ft where the fluid is being produced.
For a cold downstream environment, plug properties do not affect the maximum supportable mass flux, although plug porosity and heat transfer between gas and solid have a significant impact on the "stand-off" distance between flame and plug exit.
Results demonstrate that radiative heat transfer from a hot downstream environment to the porous plug significantly increases maximum attainable mass fluxes.
The maximum deviation is about 29% for mass flux ranging from 260 to 650 kg/m2s.
In other words, the sequences analysed are combinations of the ignition mass flux and the maximum temperature.
The maximum relative difference between the calculated mass flux and the plant data is 9.7% at 50% BMCR load.
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