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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
sÞ
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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