  Protein flotation is a process in which protein molecules are enriched by
adsorption at rising bubbles. The bubbles then form a foam above the solution,
where the liquid drains down and the dried foam, which is concentrated in
protein, is extracted. Here, the recovery rate and purity of the extract depend
on foam stability, surface coverage, bubble size, gas flow rate, etc. In this
work, we performed flotation experiments using bovine serum albumin (BSA). In
addition, an unsteady state simulation of the protein flotation process was
carried out by numerically solving the liquid drainage equation in the foam.
Thereby, the extracted liquid volume and protein concentration at the outlet
were calculated with time. Required quantities such as foam stability,
interface coverage or bubble size distribution were measured in corresponding
experiments and were fed into the model. The experiments showed that the foam
coalescence accelerates the liquid drainage leading to dryer extract and higher
protein enrichment. The modeling also reproduced the liquid recovery and
extract concentration of the flotation tests within a reasonable error range.
The modeling solely relies on experimental inputs and does not require any
tuning parameters. It can be further used for optimization or up-scaling of
protein flotation.
