2
08
L. Elsellami et al. / Applied Catalysis A: General 485 (2014) 207–213
3
8
8NH2
O
Cytosine
Uracil
1
2,5
2
1
5
5
4
2
3
NH
2
3
N
4
1
,5
1
N
H
6
O
N
6
O
7
H
7
Uracil
Cytosine
0
,5
0
Fig. 1. Structural formulas of uracil and cytosine.
0
100
200
300
Ceq (µmol/L)
400
500
600
2
. Experimental
.1. Reagents and chemicals
Pyrimidine bases uracil (Ura: C H N O ) and cytosine (Cyt:
Fig. 2. Amounts of cytosine and of uracil adsorbed per gram of TiO2 as a function of
2
−1
the equilibrium concentration Ceq on TiO2 Degussa P25 (1.25 g L ).
4
4
2
2
injection volume was 100 L and the mobile phase was H SO
2
4
C H5N O) (99% purity) were purchased from SIGMA-Aldrich and
4
3
−3
−1
(
5 × 10 mol L ).
used as received. Their formulae are given in Fig. 1. Water used
for preparation of samples was ultra-pure water, filtered through
a milli-Q PLUS 185 water system. The photocatalyst was titanium
dioxide Degussa P-25 (particle size, 20–30 nm; crystal structure,
The formation of nitrate ions was monitored using ionic
chromatography with a Dionex DX-120 pump and conductivity
detector, and an IonPac AS14A (250mm × 4 mm) column. The flow
−
1
rate was 1 mL min and the mobile phase was an alkaline buffer
(
2
−1
8
0% anatase and 20% rutile; surface area, 50 m g ).
− −1
NaHCO (1.0 mmol L ) + Na CO (8.0 mmol L )).
3 2 3
1
The formation of ammonium ions was also followed using ionic
chromatography with a Dionex DX-120 pump and conductivity
2.2. Reactor and light source
detector. The column was a CS 12A (250 mm × 4 mm). The flow
The aqueous suspensions were irradiated in a 100 mL open
−1
rate was 1 mL min and the mobile phase was H SO solutions
2
4
cylindrical reactor whose base contained an optical window with a
−1
containing 610 L L of pure sulfuric acid.
2
surface area of about 12.6 cm . The output of a Philips HPK 125 W
For all analyses the error bars are about 5%.
high mercury lamp was filtered through a circulating water cell
Computer simulations with MOPAC allowed to calculate the
(
thickness = 2.2 cm), avoiding the solution warming by IR, and a
•
frontier electron density used to determine the positions of OH
2
Corning 0.52 mW/cm filter to remove radiation with wavelength
below 340 nm. The radiant flux was measured using a VLX-3 W
radiometer with a detector CX-365 (355–375 nm).
radical attack in uracil and cytosine.
3. Results and discussion
2.3. Photocatalytic experiments
3.1. Adsorption
A volume of 20 mL of uracil and cytosine solution with dif-
In order to ensure that the adsorption process reached equilib-
rium, different concentrations of uracil and cytosine were stirred
in the dark in the presence of TiO2 and analysed as a function of
time. In both cases, the uracil and cytosine adsorptions reached
equilibrium after about 60 min.
−
1
ferent concentrations containing a concentration of 1.25 g L
of
TiO , sufficient to absorb all photons entering the photoreactor was
2
used [20]. The degradation was carried out at room temperature
◦
(
T = 25 C) and at natural pH (pH 5). The suspension was first stirred
Fig. 2(a) represents the amounts (mol g−1) of cytosine and
uracil adsorbed per gram of TiO2 as a function of the cytosine
and uracil equilibrium concentration (Ceq). In dark conditions,
the amounts of cytosine and uracil adsorbed on the TiO2 surface
(Qeq) increase with the equilibrium concentration until reaching a
plateau. The amounts of cytosine and of uracil adsorbed are iden-
tical, probably because of their similar formulae. The maximum
coverage of cytosine and uracil is about 0.03 molecule nm . This
represents about 0.6% of the maximum coverage in OH surface
groups equal to 5 OH/nm2 [21]. This value is similar to values
found for molecules containing aromatic cycles such as tryptophan,
phenylalanine [22,23].
in the dark until equilibrium adsorption was achieved. Then, the
solution was irradiated at ꢀ > 340 nm and a radiant flux equal to
2
3
.5 mW/cm . Samples taken at different times of irradiation were
filtered through 0.45 m Waters filters to remove TiO2 particles
before analyses.
2.4. Methods of analysis
−
2
The degradation of uracil and cytosine were followed by HPLC
with a Varian System equipped with a Varian Prostar 230 isocratic
pump and a Varian Prostar 330 Diode Area Detector adjusted at
2
4
9
54 nm. A Hypersil BDS C18 reverse phase column (125 mm long,
mm diameter) was used. The mobile phase was constituted by
0% of ultra-pure water containing 62 L H PO at pH 3 and 10% of
As for the majority of organic compounds [22–27], the adsorp-
tion isotherms of cytosine and uracil can be modelled using the
Langmuir approach:
3
4
−
1
methanol. The flow rate was 0.8 mL min
.
Mineralization of pyrimidine bases was monitored by deter-
mination of Total Organic Carbon (TOC) concentrations by direct
injection of the filtered samples using TOC-VCSH Shimadzu and
ASI-V Shimadzu sampler.
The carboxylic acids formed were analyzed by LC using a
Varian Prostar 230 pump, a Varian Prostar 325 UV detector
Qeq = KadsQmaxCeq(1 + KadsCeq)
Qeq is the adsorbed quantity of pollutant on the photo-
−
1
catalyst at the equilibrium (mol g ), Kads is the adsorption
−
1
constant (L mol ), Qmax is the maximum amount to be adsorbed
(
−
1
mol g ), and Ceq is the concentration of the compound at the
−
1
adsorption equilibrium (mol L ). The values of the Langmuir
parameters for cytosine and uracil are presented in Table 1.
(
(
detection at 210 nm), and a Transgenomic Icsep Coregel 87H
300 mm × 4.6 mm) column. The flow rate was 0.7 mL min . The
−
1