
 
3.2.4  Effect of the Initial Concentration of 
DBP  
The  effect  of  initial  concentration  DBP  was 
investigated  with  the  concentration  of  DBP  in  the 
catalytic  system  at  14.38-287.77  mol·L
-1
.  The 
results (Figure 9) showed that when the concentration 
of DBP<71.6 mol·L
-1
 (50mg·L
-1
), the DBP can be 
totally  degenerated  in  10  mins.  The  residue 
concentration of DBP was at g·L
-1
 to mg·L
-1
 levels 
in  the  aqueous  environment,  thus  the  present 
Fe
2
(ST)/H
2
O
2
/vis  system  can  be  used  for  the 
treatment of the DBP in the environment. 
0 20 40 60 80
20
40
60
80
100
   14.4 
   28.8  
   54.0    
   71.6 
 143.9 
 215.8 
 287.8 
Degradation percentage (%)
Reaction time (min)
 
 
umol L
-1
..
umol L
-1
.
umol L
-1
.
umol L
-1
.
umol L
-1
.
umol L
-1
.
umol L
-1
.
 
Figure 9: Effect of the initial concentration of DBP on the 
Fe
2
(ST)/H
2
O
2
/DEP catalytic degradation system. 
3.3  Reusability Investigation  
The reusable of the Fe
2
(ST)
 
was evaluated. Results 
were  shown  in  Figure  10,  which  indicated  that  
Fe
2
(ST)  could  be  used  for  at  least  10  cycles  with 
degradation rate higher than 95% upon recovery on 
average.  No  obvious  decrease  in  the  degradation 
efficiency and iron leaching were found. Compared 
with  literature  reports,  the  Fe
2
(ST)  is  a  potential 
effective and reusable catalyst for the degradation of 
DBP with high degradation effect. 
-1 0 1 2 3 4 5 6
0
20
40
60
80
100
 (a)             (b)
Degradation percentage (%)
Cycle number
 
 
 
Figure 10: Recycle of the Fe
2
(ST) catalyst (a) Method 1: 
re-adding  DBP  after  rotating  evaporation  of  the 
post-degeneration solution, (b) Method 2: re-adding DBP 
directly in the post-degeneration solution. 
4  CONCLUSIONS 
In this work, a binuclear iron (III) complex (Fe
2
(ST)) 
was  prepared  and  characterized  by  EA,  TG/DTG, 
UV/Vis and FTIR, etc. It was used as a catalyst for 
the Fenton–like reaction of the catalytic degradation 
of  the  emerging  contaminants  di-butyl-phthalate 
(DBP). It is found that  under the condition of visible 
light,  the  catalytic  degradation  of  DBP  could  be 
achieved  by  Fe
2
(ST)/H
2
O
2
  system  in  aqueous 
solution with the pH range from 3.5 to 8.0. Compared 
with ordinary Fenton reaction system, a wide range of 
pH value for the degradation of DBP achieved. The 
degradation of DBP was more than 99% when the 
concentration  of  Fe
2
(ST)  was  larger  than  5.50 
mol·L
-1
, the concentration of H
2
O
2
 was larger than 
8.16  mmol·L
-1
,  and the  concentration of  DBP  was 
less than 20.0 mg·L
-1 
. With the aid of the electronic 
spectrum monitoring, it is found  that the transition 
state of -N bridged bi-nucleus Fe(III)-H
2
O
2
 centre 
may form in the catalytic process.  
ACKNOWLEDGEMENTS 
We would like to thank the National Natural Science 
Foundation  of  China  (51608479,  81502421),  the 
National  Natural  Science  Foundation  of  Zhejiang 
Province  (LY14B04003),  the  National  Natural 
Science Foundation of Ningbo (2018A610206), the 
National  College  Students’  innovation  and 
entrepreneurship training program (201813022009), 
the  Xinmiao  Students’  innovation  training  program 
of  Zhejiang  Province  (2018R401181)  for  the 
financial support. 
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33