Environmental Engineering Reference
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(ii): Two-phase water outlet flow
Flow direction
(iii) : Liquid exit flow
(i): Liquid inlet flow
Fig. 2 Liquid water mass conservation illustration
V w,i
V w,e
h w,i
h w,e
Fig. 3 Water level and velocity at inlet and exit
conservation in Eq. ( 7 ) must be employed. Figure 2 illustrates the mass conser-
vation region in control volume for each term in Eq. ( 8 ).
Q m ; w ; i
¼ Q m ; w ; b
þ Q m ; w ; e
ð
8
Þ
ð
i
Þ
ð
ii
Þ
ð
iii
Þ
where Q denotes volumetric
fl
flow rate, and the term (i) is measured directly from the
fl
flow meter as displayed in Fig. 3 . The term (iii) is the volumetric
fl
flow rate of
the sum of the dispersed liquid water particles in the two-phase
fl
flow exiting the
channel. The term (iii) is the volumetric
flow rate exiting the channel and is
approximated by calculating the mean water exit velocity and boundary height. The
extent of dispersed liquid water is a good indicator of breakup; however, it is not
easy to measure dispersed liquid water or Q m,w,b directly; therefore the measure-
ment needs to be carried out by subtracting measured value of liquid inlet
fl
fl
ow by
exit
fl
flow. The volumetric
fl
flow rate of inlet and exit are de
ned in Eqs. ( 9 ) and ( 10 ).
Q m ; w ; i ¼ h w ; i v w ; i Y
ð
9
Þ
Q m ; w ; e ¼ h w ; e v w ; e Y
ð
10
Þ
where h w,i , h w,e ,v w,i , and v w,e are water level of channel and water velocity of inlet
and exit, respectively. The Y in Eqs. ( 9 ) and ( 10 ) is the width of the
fl
flow channel.
The illustration of the mass
flow component in both equations is shown in Figure 3 .
Since Q m,w,i and Q m,w,e are known, Q m,w,b can be calculated which permits the
introduction of the breakup ratio B as expressed as:
fl
 
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