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composed of a salt and water. The general formula for acid
base neutralization
-
reactions can be written as:
acid
þ
base
!
salt
þ
water
ð
28
Þ
The process of pH neutralization (see Fig. 5 ) is constituted essentially of a
treatment tank of cross sectional area A, a mixer, acid and base injection pipes, a pH
probe, a level sensor to measure the level h in the tank and a discharge valve
(Henson and Seborg 1994 ; Salehi et al. 2009 ). It consists of an acid stream q 1 ,
buffer stream q 2 and base stream q 3 that are mixed in the tank. The ef
uent stream
q 4 exits the tank via the discharge valve with an adjusted pH m . The streams q fg
fl
4
i
¼
1
are characterized by the following parameters:
4
i
4
i
W a fg
1 are the charge related quantities for qif fg
1 .
￿
¼
¼
4
i¼1 are the mass balance quantities for qif fg
4
i¼1 .
W b fg
￿
The pH probe introduces a delay time
s
in the measured pH m value such as
pH m ¼
.
The objective of the pH neutralization process is to control the pH value of the
pH
ð
t
ef
fl
uent through manipulating the base
fl
ow rate q 3 while considering the acid
fl
ow
rate q 1 and the buffer
ow rate q 2 as disturbances.
The dynamic model of the neutralization process is developed as follows:
fl
The pH value of the obtained solution is derived from the conservation equa-
tions and equilibrium reactions as follows:
￿
K a1
H þ
2K a1 K a2
H þ
þ
K w
H þ
½
2
½
H þ
W a4 þ
þ
W b4
2
½
¼
0
:
ð
29
Þ
K a1
H þ
K a1 K a2
H þ
½
1
þ
þ
½
½
Fig. 5 A pH neutralization
process
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