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You can use plain HTML placeholders to indicate where the dynamic data should be dropped from the Bindings panel.

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11-135 Heat Transfer Heat transfer in the turbulent regime is essentially a macromixing process Heat transfer coef cients are controlled by the turbulence levels (hence boundary layer thickness) near the heat transfer surfaces In many cases the process demands of suspension or dispersion and mass transfer are more than suf cient to ensure adequate heat transfer 11-136 Solid Particles Particle suspension from the base and drawdown from the surface are often required in gas liquid agitated vessels and are in uenced in a complex manner by gassing There are no well-established correlations for the in uence of gas Particle suspension is probably controlled by the energy and frequency of turbulent bursts, and drawdown by details of local ow patterns and vorticity at the surface, both of which could be expected to be affected by the presence of gas bubbles 11-137 Flow Patterns.

Flow patterns can be important A slow reaction scheme (occurring in the bulk liquid) with competing steps may exhibit selectivity dependent on the local concentration of a liquid or dissolved gas reactant In this case the liquid ow pattern (ie, whether the liquid undergoes backmixing or plug ow or, as is almost always the case, somewhere in between) is important A fast reaction scheme (occurring mainly near the gas liquid interface) with dependence of selectivity on local dissolved gas concentration, will be sensitive to the history of gas concentration in the bubbles as they travel through the reactor In other words, the selectivity will be sensitive to the degree of backmixing of the gas phase, and therefore to the bubble ow pattern Even for simple gas liquid mass transfer, the gas ow pattern is critical unless a very small proportion of the dissolvable gas is absorbed per pass.

The Text Flow options determine the direction of text as it flows from one section to the next. You may choose between text that starts along the top row and flows from left to right and then goes to the next lowest row, flowing from left to right, etc. The second option is to have text start in the left column, flowing from top to bottom, and then to the next column to the right, flowing from top to bottom. Clicking the Preview check box displays changes as you make them in the Area Type Options dialog box.

For example, if 95% of the inlet dissolvable gas is absorbed, its mean concentration in the gas phase (and hence its mean transfer rate to the liquid), if in plug ow, is 517 times that for an perfectly backmixed gas phase Here a con ict can arise in an agitated vessel High power input per unit mass is required to enhance mass transfer area and heat transfer coef cient, but this will result in a high degree of gas recirculation, reducing the mean gas phase concentration driving force for mass transfer Local shear rates will also increase with power input The balance will vary with scale 11-2 SELECTION AND CONFIGURATION OF GAS LIQUID EQUIPMENT.