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°®ÓëÓêÏÂ(½ð±Ò+2): 2011-10-20 08:48:17
milk_HH(½ð±Ò+15, ·­ÒëEPI+1): 2011-10-20 10:30:41
So far, most researchers have adopted regular vertical foam separation column. During the process of foam separation, bubbles in foam phase move from bottom to top along the column axis and partial liquid between bubbles (Plateau boundary and nodes) moves from top to bottom, that is, inner flow. The bubbles and inner-flow liquid are in reverse flow in entire height of foam phase, so they experienced big flow friction. With separation concentration increasing, especially those biological components such as protein, the friction gets larger and draining of foam phase is harder. Then the speed of foam interspace liquid in column reaches balance in high liquid hold, so it is hard to raise enrichment ratio of foam separation.
2Â¥2011-10-20 08:15:41
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shrimp5555

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milk_HH(½ð±Ò+10): 2011-10-21 08:46:23
Until now what the majority researchers use is the conventional vertical froth separation tower, in this tower foam separation process, froth air bubble along tower axial by the under upward movement, but between the air bubble partial liquids (the Plateau boundary layer and node place) is the internal reflux by on downward movement, between the air bubble and the internal reflux liquid is at the adverse current condition in the froth entire altitude, therefore between them the flow resistance is big. Along with separates the component density to increase is the biological component like protein specially, the flow resistance is bigger, causes the froth to arrange the fluid to be more difficult, in the tower the froth gap fluid's flow rate in high holds the liquid volume to issue balanced, thus enhances the foam separation to concentrate the ratio with difficulty.
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