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Basics of Fluid Mechanics, 2014a

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13.5. CLASSIFICATION OF LIQUID-LIQUID FLOW REGIMES 539<br />

materials flow in the opposite direction, it is referred as counter–current. In general,<br />

the co-current is the more common. Additionally, the counter–current flow must have<br />

special configurations <strong>of</strong> long length <strong>of</strong> flow. Generally, the counter–current flow has a<br />

limited length window <strong>of</strong> possibility in a vertical flow in conduits with the exception <strong>of</strong><br />

magnetohydrodynamics. The flow regimes are referred to the arrangement <strong>of</strong> the fluids.<br />

The main difference between the liquid–liquid flow to gas-liquid flow is that gas<br />

density is extremely lighter than the liquid density. For example, water and air flow as<br />

oppose to water and oil flow. The other characteristic that is different between the gas<br />

flow and the liquid flow is the variation <strong>of</strong> the density. For example, a reduction <strong>of</strong> the<br />

pressure by half will double the gas volumetric flow rate while the change in the liquid<br />

is negligible. Thus, the flow <strong>of</strong> gas–liquid can have several flow regimes in one situation<br />

while the flow <strong>of</strong> liquid–liquid will (probably) have only one flow regime.<br />

13.5.1 Co–Current Flow<br />

In Co–Current flow, two liquids can have three main categories: vertical, horizontal,<br />

and what ever between them. The vertical configuration has two cases, up or down.<br />

It is common to differentiate between the vertical (and near vertical) and horizontal<br />

(and near horizontal). There is no exact meaning to the word “near vertical” or “near<br />

horizontal” and there is no consensus on the limiting angles (not to mention to have<br />

limits as a function with any parameter that determine the limiting angle). The flow<br />

in inclined angle (that not covered by the word “near”) exhibits flow regimes not much<br />

different from the other two. Yet, the limits between the flow regimes are considerably<br />

different. This issue <strong>of</strong> incline flow will not be covered in this chapter.<br />

13.5.1.1 Horizontal Flow<br />

The typical regimes for horizontal flow<br />

are stratified flow (open channel flow,<br />

and non open channel flow), dispersed<br />

bubble flow, plug flow, and annular flow.<br />

For low velocity (low flow rate) <strong>of</strong> the<br />

two liquids, the heavy liquid flows on the<br />

bottom and lighter liquid flows on the<br />

top 5 as depicted in Figure 13.2. This<br />

Light Liquid<br />

Heavy Liquid<br />

Fig. -13.2. Stratified flow in horizontal tubes<br />

when the liquids flow is very slow.<br />

kind <strong>of</strong> flow regime is referred to as horizontal flow. When the flow rate <strong>of</strong> the lighter<br />

liquid is almost zero, the flow is referred to as open channel flow. This definition (open<br />

channel flow) continues for small amount <strong>of</strong> lighter liquid as long as the heavier flow can<br />

be calculated as open channel flow (ignoring the lighter liquid). The geometries (even<br />

the boundaries) <strong>of</strong> open channel flow are very diverse. Open channel flow appears in<br />

many nature (river) as well in industrial process such as the die casting process where<br />

liquid metal is injected into a cylinder (tube) shape. The channel flow will be discussed<br />

in a greater detail in Open Channel Flow chapter.<br />

5 With the exception <strong>of</strong> the extremely smaller diameter where Rayleigh–Taylor instability is an important<br />

issue.

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