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Basics of Fluid Mechanics, 2014a

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13.6. MULTI–PHASE FLOW VARIABLES DEFINITIONS 543<br />

13.5.1.3 Vertical Flow Under Micro Gravity<br />

The above discussion mostly explained the<br />

flow in a vertical configuration when the<br />

surface tension can be neglected. In cases<br />

where the surface tension is very important.<br />

For example, out in space between gas and<br />

liquid (large density difference) the situa-<br />

Liquid Flow Rate<br />

Dispersed<br />

Bubble<br />

Trickling<br />

Flow<br />

Pulsing<br />

Gas Flow Rage<br />

Pulsing &<br />

Bubbling<br />

Spray or<br />

Mist Flow<br />

Dispersed<br />

Bubble<br />

Fig. -13.7. A dimensional vertical flow map<br />

under very low gravity against the gravity.<br />

tion is different. The flow starts as dispersed<br />

bubble (some call it as “gas continuous”)<br />

because the gas phase occupies<br />

most <strong>of</strong> column. The liquid flows through<br />

a trickle or channeled flow that only partially<br />

wets part <strong>of</strong> the tube. The interaction<br />

between the phases is minimal and can be<br />

considered as the “open channel flow” <strong>of</strong><br />

the vertical configuration. As the gas flow<br />

increases, the liquid becomes more turbulent<br />

and some parts enter into the gas phase as drops. When the flow rate <strong>of</strong> the gas<br />

increases further, all the gas phase change into tiny drops <strong>of</strong> liquid and this kind <strong>of</strong><br />

regime referred to as mist flow. At a higher rate <strong>of</strong> liquid flow and a low flow rate <strong>of</strong><br />

gas, the regime liquid fills the entire void and the gas is in small bubble and this flow<br />

referred to as bubbly flow. In the medium range <strong>of</strong> the flow rate <strong>of</strong> gas and liquid,<br />

there is pulse flow in which liquid is moving in frequent pulses. The common map is<br />

based on dimensionless parameters. Here, it is presented in a dimension form to explain<br />

the trends (see Figure 13.7). In the literature, Figure 13.7 presented in dimensionless<br />

coordinates. The abscissa is a function <strong>of</strong> combination <strong>of</strong> Froude ,Reynolds, and Weber<br />

numbers. The ordinate is a combination <strong>of</strong> flow rate ratio and density ratio.<br />

Flow With The Gravity<br />

As opposed to the flow against gravity, this flow can starts with stratified flow. A<br />

good example for this flow regime is a water fall. The initial part for this flow is more<br />

significant. Since the heavy liquid can be supplied from the “wrong” point/side, the<br />

initial part has a larger section compared to the flow against the gravity flow. After the<br />

flow has settled, the flow continues in a stratified configuration. The transitions between<br />

the flow regimes is similar to stratified flow. However, the points where these transitions<br />

occur are different from the horizontal flow. While this author is not aware <strong>of</strong> an actual<br />

model, it must be possible to construct a model that connects this configuration with<br />

the stratified flow where the transitions will be dependent on the angle <strong>of</strong> inclinations.<br />

13.6 Multi–Phase Flow Variables Definitions<br />

Since the gas–liquid system is a specific case <strong>of</strong> the liquid–liquid system, both will be<br />

united in this discussion. However, for the convenience <strong>of</strong> the terms “gas and liquid”<br />

will be used to signify the lighter and heavier liquid, respectively. The liquid–liquid (also

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