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Bioresource Technology 96 (2005) 897–906
Dechlorination of chlorophenols found in pulp bleach plantE-1 effluents by advanced oxidation processes
Rui Wang a,b, Chen-Loung Chen a,*, Josef S. Gratzl a
a Department of Wood and Paper Science, North Carolina State University, Raleigh, North Carolina 27695-8005, USAb Mead-Westvaco Corporation, Covington mill, Covington, Virginia 24426, USA
Received 28 April 2003; received in revised form 26 August 2004; accepted 26 August 2004
Available online 26 October 2004
Abstract
Studies were conducted on the response of 2,4,6-trichlorophenol (1), 2,3,4,5-tetrachloro-phenol (2) and 4,5-dichloroguaiacol (3)
toward advanced oxidation processes, such as UV-, O2/UV-, H2O2/UV-, O3/UV- and O3–H2O2/UV-photolyses with irradiation of
254nm photons. The compounds 1–3 are among the chlorophenols found in the Kraft-pulp bleach plant E-1 effluents. The studies
were extended to treatment of these compounds with ozonation and O3–H2O2 oxidation systems in alkaline aqueous solution.
Except for the O2/UV-photolysis of 1 and H2O2/UV-photolysis of 2, the dechlorination of 1–3 by O2/UV- and H2O2/UV-potolyses
were less effective than the corresponding N2/UV-potolysis of 1–3. Guaiacol-type chlorophenols were more readily able to undergo
dechlorination than non-guaiacol type chlorophenols by N2/UV-, O2/UV- and H2O2/UV-potolyses. In addition, the efficiency
for the dechlorination of 1–3 by N2/UV-, O2/UV- and H2O2/UV-potolyses appeared to be dependent upon the inductive and
resonance effects of substituents as well as number and position of chlorine substituent in the aromatic ring of the compounds.
The dechlorination of 2 by treatment with O3 alone is slightly more effective than the corresponding the O3/UV-photlysis, whereas
the dechlorination of 2 by treatment with the combination of O3 and H2O2 was slightly less effective than the corresponding
O3–H2O2/UV-photolysis. In contrast, the dechlorination of 3 on treatment with O3 alone was slightly less effective than the corre-
sponding the O3/UV-photolysis, whereas the dechlorination of 3 on treatment with the combination of O3 and H2O2 was slightly
more effective than the corresponding the O3–H2O2/UV-photolysis. In the dechlorination of 2 and 3, chemical species derived from
ozone and hydrogen peroxide in alkaline solution were dominant reactions in the O3/UV- and O3–H2O2/UV-photolysis systems as in
the O3 and O3–H2O2 oxidation systems. Possible dechlorination mechanisms involved were discussed on the basis of kinetic data.
� 2004 Elsevier Ltd. All rights reserved.
Keywords: Chlorinated phenols; Advanced oxidation processes; UV-photolysis; Dechlorination; Kinetics; Oxygen; Hydrogen peroxide; Ozone
1. Introduction
In the kraft pulping, the resulting crude pulp usuallycontains approximately 3% of residual lignin (Marton,
1971). The crude kraft pulp is then treated successively
with elemental chlorine under acidic condition (C stage),
extracted with an alkaline solution (E-1 stage), hydrogen
peroxide (P stage), then twice with chlorine dioxide (DD
0960-8524/$ - see front matter � 2004 Elsevier Ltd. All rights reserved.
doi:10.1016/j.biortech.2004.08.011
* Corresponding author. Tel.: +1 919 515 5749; fax: +1 919 515
6302.
E-mail address: [email protected] (C.-L. Chen).
stage), i.e., bleaching sequence CEPDD (Dence and
Annergren, 1979; Gellerstedt and Zhang, 2001; Rajan
et al., 1996) to remove the bulk of the residual ligninto enhance rightness. In the previous investigation,
bleaching plant E-1 effluent from bleaching of Loblolly
pine kraft pulp with a bleaching sequence CEPDD
was found to contain considerable color carriers con-
tribute to its color, 13,000 Co–Pt units (Wang et al.,
2003). The total solid of the effluent was 5.6g/l, of which
3.5 and 2.1g/l are organic and inorganic materials,
respectively. The total chlorine content of the effluentwas 957mg/l, of which 689 and 268mg/l are chloride
OH
Cl
ClCl
OH
Cl
Cl
ClCl
OH
Cl
OCH3
Cl
1 2 3
Fig. 1. Structure of 2,4,6-trichlorophenols (1), 2,3,4,5-phenol (2) and
4,5-dichloroguaiacol (3).
898 R. Wang et al. / Bioresource Technology 96 (2005) 897–906
(Cl�) and organically bound chlorine (OCl), respec-
tively. Approximately 5% of the OCl were ether-extract-
able. Thus, it is evident that the major part of the OCl is
present in the high relative molecular mass fractions that
are not extractable by ether.
Furthermore, it was found that the N2/UV-photolysis
did not be appreciable effectiveness in color reduction
and removal of OCl in the E-1 effluent. Addition ofhydrogen peroxide promoted the reduction of color car-
riers and degradation of polychlorinated oxylignins
(PCOLs), but did not improve appreciably in the
dechlorination. However, introduction of ozone stream
into the UV-photolysis system resulted in appreciable
improvement in both the decolorization and dechlorina-
tion of E-1 effluent. Up to approximately 40% of the
total organically bound chlorine (TOCl) in these sub-strates were converted into chloride ion within reaction
time of 5min. Therefore, the objective of such as UV-,
O2/UV-, O3/UV- and O3–H2O2/UV-photolyses with
irradiation of 254nm photons. This investigation is to
elucidate possible reaction mechanisms by studying the
kinetics for dechlorination of chlorophenols identified
in the E-1 effluent by advanced oxidation processes,
Because 2,3,4,5-tetrachlorophenol (2) and 4,5-dichloro-guaiacol (3) are identified as the major components of
chlorinated phenols in the E-1 effluent, they were
selected as model compounds in this study (see Fig. 1
for structures). In addition, 2,4,6-trichlorophenol (1)
was also selected since it is shown to be a potential pre-
cursor for the formation of dioxin in the conventional
chlorine bleaching (Hruford and Negri, 1992; Rajan
et al., 1994, 1996), although the E-1 effluent contains itin rather small amount.
2. Methods
2.1. Chlorophenols
2,4,6-Trichlorphenol (mp 79–80 �C) and 2,3,4,5-tetrachlorophenol (mp 116–7 �C) were purchased from
Aldrich Chemical Inc., Milwaukee, WI, USA and 4.5-
dichloroguaiacol (mp 68–70 �C) from Helix Biotech.
Corp., Toronto, Ontario, Canada. These phenols were
recrystallized from CHCl3–petroleum ether to con-
stant mp.
2.2. Ozone
Ozone was prepared by passing oxygen through an
ozone generator (Model T-816, Polymetric, Inc. San
Jose, CA, USA) at a constant power. The concentration
of ozone produced was controlled at the range of either2.0–2.5% or 4.0–4.5% depending on the requirement of
particular studies. The concentration of the ozone
stream was constantly monitored with an ozone monitor
(Model HC, PCI Ozone and Control System, Inc. West
Caldwell, NJ, USA) before sending to the reactor.
2.3. UV-photolysis
Thin film reactor (Ace Glass Laboratories, Vineland,
NJ, USA) used in this study was made of borosilicate
glass and equipped with a weir arrangement to provide
a flow of reactant solution over a knife-edge and down
the inner wall of the reactor. An impeller type fluid
pump with adjustable pumping capacity was provided
to circulate the effluent through the reactor. A low
pressure Hg lamp, 12W with energy profile of approxi-mately 3.4W at 254nm was held vertically and sur-
rounded by a water-cooled jacket. In this study, the
volume of the E-1 effluent, and the solution of selected
model compounds with concentration of 0.5mM in
0.01M NaOH were 400ml with a circulation rate of
250ml/min. The flow rate of both O2 and O3 streams
were either 50 or 100ml/min when applied to the system.
Introduction of 4.5% O3 stream with flow rate of 50ml/min for 1min corresponds to approximately 0.1mmol of
O3. The amount of substrate in 400ml of the 0.5mM
solution is 0.2mmol. The 3.5% O3 stream with flow rate
of 400ml/min for one min corresponds to O3 charge of
30mg/min. In the case of studies under N2 atmosphere,
N2 was introduced into the reactor at 1 l/min for at least
1h to assure completion of air displacement. The pH of
the solution was monitored through the entire reactionperiod. Samples were withdraw at certain intervals from
the sample port and injected into ion chromatography,
Dionex 2010i (Dionex Corp. Sunnyvale, CA, USA),
equipped with an anion separator column AS-4 to ana-
lyze and quantify the chloride anion formed during
dechlorination.
3. Results and discussion
Alkaline solutions of 2,4,6-trichlorophenol (1),
2,3,4,5-tetrachlorophenol (2) and 4,5-dichloroguaiacol
(3) (0.5mM in 0.01M NaOH solution) were initially
irradiated with 254nm photons under nitrogen atmos-
phere with an initial pH of 10.34. The dechlorination
was monitored by quantitative determination of chlo-ride anion formed, the results of which were used as
standards. The UV-photolyses were then carried out
y = 100e
y = 100e
y = 100e
-0.0027x
R2 = 0.9806
-0.0036x
R2 = 0.9938
-0.0055x
R2 = 0.956
0
20
40
60
80
100
120
0 20 40 60 80 100 120 140
UV-Irradiation Time (min)
Org
anic
ally
Bou
nd C
hlor
ine
Con
tent
(Mol
% p
er O
rigi
nal)
Fig. 3. Effect of oxidants on dechlorination of 2,4,6-trichlorophenol
(1) on UV-photolysis with 254nm photons. Under nitrogen atmos-
phere: (-j-j-); under oxygen atmosphere: (-m-m-); with H2O2 under
nitrogen atmosphere (H2O2 charge: 100% on substrate by weight).
Initial pH: 10.34; temperature: ambient; UV source: 12W low pressure
Hg lamp (254nm photons).
y = 100e-0.0015x
R2 = 0.9823
y = 100e-0.0031x
R2 = 0.9665
y = 100e-0.0033x
R2 = 0.9445
y = 100e-0.2084x
R = 0.9852
20
40
60
80
100
120
Org
anic
ally
Bou
nd C
hlor
ine
Con
tent
(Mol
% p
er O
rigi
nal)
R. Wang et al. / Bioresource Technology 96 (2005) 897–906 899
under oxygen atmosphere and with hydrogen peroxide
(H2O2 charge of 2% on substrate by weight) under nitro-
gen atmosphere. In addition, comparative studies were
conducted on the dechlorination of 2 and 3 in alkaline
solution with ozone (O3 charge of 0.1mol/min) and the
combination of ozone and hydrogen peroxide (O3
charge of 0.1mol/min and H2O2 charge of 2% on sub-
strate by weight, respectively). The O3/UV- and O3–
H2O2/UV-photolyses of 2 and 3 were carried under the
same condition as the treatment of these compounds
with ozone, and with combination of ozone and hydro-
gen peroxide under aerial atmosphere. Based on the re-
sults it appeared that the responses of 1–3 towards the
UV-photolysis systems with 254nm photons and theoxidant systems alone were different (Figs. 2–5 and 8
and 9, Table 1). Nevertheless, the kinetics of the dechlo-
rination for the chlorophenols investigated were all first
order with respect to the organically bound chlorine
(OCl) in the substrate. The dechlorination rate constants
of these reactions are summarized in Table 1.
3.1. UV-photolysis under nitrogen atmosphere
Compound 3 readily undergoes dechlorination in
alkaline solution with the first order reaction rate con-
stant of 1.8 · 10�4 s�1 by N2/UV-photolysis (Fig. 2,
Table 1). By contrast, the dechlorination rate constant
of 2 is the slowest among the compounds investigated
with the rate constant of 0.43 · 10�4 s�1 under the same
reaction condition. Legrini et al. (1993) postulated thathydroxyl radicals (HO�) are responsible for oxidation
of organic compounds, such as dechlorination of chloro-
phenols, by UV-photolysis with 254nm photons in the
presence of added oxidants. The hydroxyl radical is a
y = 100e-0.0026x
R2 = 0.9331
y = 100e-0.0036x
R2 = 0.995
y = 100e-0.0108x
R2 = 0.9967
0
20
40
60
80
100
120
0 20 40 60 80 100 120 140
UV-Irradiation Time (min)
Org
anic
ally
Bou
nded
Chl
orin
e C
onte
nt(M
ol %
per
Ori
gina
l)
Fig. 2. Dechlorination of chlorophenolics on UV-photolysis with
254nm photons under nitrogen atmosphere. 2,4,6-Trichlorophenol (1)
(-�-�-); 2,3,4,5-tetrachlorophenol (2) (-j-j-), and 4,5-dichloroguaia-
col (3) (-m-m-). Initial pH: 10.34; temperature: ambient; UV source:
12W low pressure Hg lamp (254nm photons).
00 50 100 150 200
UV-Irradiation Time (min)
Fig. 4. Effect of oxidants on dechlorination of 2,3,4,5-tetrachlorophe-
nol (2) on UV-photolysis with 254nm photons. Under nitrogen
atmosphere: (-j-j-); under oxygen atmosphere: (-m-m-); with H2O2
under nitrogen atmosphere (H2O2 charge: 2% on substrate by weight);
with O3 under aerial atmosphere: (-d-d-) (O3 charge: 0.1mmol/min).
Initial pH: 10.34; temperature: ambient; UV source: 12W low pressure
Hg lamp (254nm photons).
very strong oxidant with reox potential of 2.80V. Since
water does not absorb 254nm photons, it is not a source
of hydroxyl radicals in the N2/UV-photolysis of 1, 2 and
3 without added oxidants. Thus, as demonstrated in our
previous work (Thomas et al., 1995), the only direct
pathway to dechlorinate the substrates is the homolytic
cleavage of Ar–Cl bond in the phenoxide anion, Clx-(ph-
O�), of the substrates in alkaline solution, producing thecorresponding p-and o-aryl radical species of the type
Cl(x�1)-(�O-ph�) and chlorine radicals (Cl�) from 1, p-,
m- and o-aryl radical species and chlorine radicals from
y = 100e-0.1672x
R = 0.99012
y = 100e -0.0108x
R = 0.99672
y = 100e-0.0099x
R = 0.99812
y = 100e-0.009x
R2 = 0.9987
0
20
40
60
80
100
120
0 20 40 60 80 100 120 140
Reaction Time (min)
Org
anic
ally
Bou
nd C
hlor
ine
Con
tent
(Mol
% p
er O
rigi
nal)
Fig. 5. Effect of oxidants on dechlorination of 4,5-dichloroguaiacol (3)
on UV-photolysis with 254nm photons. Under nitrogen atmosphere:
(-j-j-); under oxygen atmosphere: (-m-m-); with H2O2 under
nitrogen atmosphere (H2O2 charge: 2% on substrate by weight); with
O3 under aerial atmosphere: (-d-d-) (O3 charge: 0.1mmol/min). Initial
pH: 10.34; temperature: ambient; UV source: 12W low pressure Hg
lamp (254nm photons).
900 R. Wang et al. / Bioresource Technology 96 (2005) 897–906
2, and p-, and m-aryl radical species and chlorine radi-
cals from 3. These aryl radical species derived from 1,2 and 3 would behave chemically in several ways in alka-
line solutions under nitrogen atmosphere. For example,
these radical species could undergo recombination with
chlorine radicals to regenerate the starting substrates
and polymerization to produce the corresponding bi-
phenyl derivatives (Thomas et al., 1995). In addition,
according to McElroy (1990), the chlorine radicals pro-
duced can oxidize water molecules to produce hydroxylradicals (HO�) because of the large molarity of H2O (liq)
present in the reaction system. The chlorine radicals
(Cl�) are in turn reduced to chloride anions (Cl�).
On the basis of observed dechlorination rate con-
stants and the structures of chlorophenols 1, 2 and 3,
Table 1
Rate constants for dechlorination of 2,4,6-trichlorophenols (1), 2,3,4,5-ph
photons with and without added oxidants, and by hydrogen peroxide, ozon
Oxidation system and chemicals
added to the reaction mixtureaDechlorination r
2,4,6-Trichloroph
UV-photolysis under nitrogen atmosphere 0.6 · 10�4 s�1
UV-photolysis under oxygen atmosphere 0.92 · 10�4 s�1
H2O2/UV-photolysisb under nitrogen atmosphere 0.45 · 10�4 s�1c
Oxidation with O3d under aerial atmosphere NDe
O3/UV-photolysisd under aerial atmosphere NDe
Oxidation with O3d and H2O2
b under aerial atmosphere NDe
O3–H2O2/UV-photolysis b,d under aerial atmosphere NDe
a Substrate solution: 400ml with concentration of 0.5mM in 0.1M NaOHb Hydrogen peroxide charge: 2% on substrate in weight.c Hydrogen peroxide charge: 100% on substrate in weight.d Ozone stream of with ozone concentration of 4.5% with flow rate of 50e ND = not determined.
the dechlorination rate seems to be dependent upon
the inductive and resonance effects of substituents in
addition to the initial concentration of the substrate.
In terms of an inductive effect, phenolic hydroxyl group
and aromatic methoxyl groups are electron releasing
groups, which activate the aromatic ring. In contrast,chlorine group is the electron attracting group that
deactivates the aromatic ring. Furthermore, the dechlo-
rination rate is also affected by the number and orienta-
tion of chlorine substituents with respect to phenolic
hydroxyl group in the aromatic ring of the compounds.
3.2. UV-photolysis under oxygen atmosphere
The UV-photolysis of chlorophenols 1, 2 and 3 with
254nm photons was carried out in alkaline solution
under oxygen atmosphere. Except for the oxygen atmos-
phere, the reaction condition is the same as the corre-
sponding N2/UV-photolysis. The first order reaction
rate constant for dechlorination of 1 is increased as com-
pared to that by N2/UV-photolysis, from 0.6 · 10�4 s�1
to 0.92 · 10�4 s�1 (Fig. 3, Table 1). In contrast, thedechlorination rate constants for 2 and 3 are decreased,
from 0.43 · 10�4 s�1 to 0.23 · 10�4 s�1 (Fig. 4, Table 1)
and from 1.8 · 10�4 s�1 to 1.5 · 10�4 s�1 (Fig. 5, Table
1), respectively.
Conceivably, in the O2/UV-photolysis of 1, 2 and 3 in
alkaline solution, the resulting p-, m- and o-aryl radical
species of the type Cl(x�1)-(�O-phÆ) derived from the
homolytic cleavage of Ar–Cl bonds in the correspondingphenoxide anions of the type Clx-(ph-O
�) react with the
dissolved molecular oxygen to form the corresponding
unstable polychlorinated p-, m- and o-phenoxide anion
peroxyl radical species of the type Cl(x�1)-(�O-ph-O-
O�) in addition to the reactions involving in the dechlo-
rination of these compounds in alkaline solution by N2/
photolysis as discussed in the previous section. Since the
O2 concentration in the O2-saturated solution (1.29mM
enol (2) and 4,5-dichloroguaiacol (3) by UV-photolysis with 254nm
e and hydrogen peroxide-ozone
ate constants (j)
enol (1) 2,3,4,5-Tetrachlorophenol (2) 4,5-Dichloroguaiacol (3)
0.43 · 10�4 s�1 1.8 · 10�4 s�1
0.23 · 10�4 s�1 1.5 · 10�4 s�1
0.43 · 10�4 s�1b 1.65 · 10�4 s�1b
3.74 · 10�3 s�1 2.72 · 10�3 s�1
3.47 · 10�3 s�1 2.8 · 10�3 s�1
3.47 · 10�3 s�1 2.95 · 10�3 s�1
3.91 · 10�3 s�1 2.8 · 10�3 s�1
, corresponding to 0.2mmol substrate.
ml/min, corresponding to ozone charge of 0.1mmol/min.
R. Wang et al. / Bioresource Technology 96 (2005) 897–906 901
at 25 �C) is greater than the initial substrate concentra-
tion (0.5mM) (Thomas et al., 1995), the reactions lead-
ing to the formation of the polychlorinated phenoxide
anion peroxyl radical species is a dominant reaction in
the UV-photolysis under oxygen atmosphere. The
resulting p- and o-phenoxide anion peroxyl radical spe-cies, 4 and 6 derived from 1 would immediately undergo
hydrolysis to the corresponding p-and o-benzoquinone
derivatives, 5 and 7, with concomitant formation of hyd-
roxyl radicals (HO�), respectively (Fig. 6). In contrast,
the m-phenoxide anion peroxyl radical species derived
from 2 and 3 undergo hydrolysis to produce resorcinol
derivatives, such as 9 from 2d via the corresponding
and o-phenoxide anion peroxyl radical species 8, withconcomitant formation of hydroxyl radicals (HO�)
(Schuchmann and Sonntag, 1987). Moreover, 5 and 7
would further undergo dechlorination by nucleophilic
attack of hydroxide anion (HO�) at C-b of a,b-unsatu-
Fig. 6. Possible reaction mechanisms for dechlorination of 2,4,6-trichloroph
photolysis with 254nm photons under oxygen atmosphere.
rated ketone moiety in these products to give the corre-
sponding chlorohydrol intermediates 10 and 12,
followed by b-elimination of chloride ion to give the cor-
responding phenoxide anion of 4-hydroxy-6-chloro-p-
quninone (11) and 2-hydroxy-6-chloro-o-quninone
(13), respectively (Fig. 6). It is noteworthy that 11 and13 are interconverting via tautomerism. The resulting
o- and p-quinone derivatives would further undergo oxi-
dative degradation under the reaction condition.
3.3. UV-photolysis with hydrogen peroxide under
nitrogen atmosphere
The dechlorination rates for compounds 1, 2 and 3varied when their alkaline solutions were irradiated with
254nm photons in the presence of hydrogen peroxide
under nitrogen atmosphere. In the dechlorination of
1, when hydrogen peroxide charge of 100% on the
enol (1) and 2,3,4,5-tetrachloropehnol (2) in alkaline solution by UV-
902 R. Wang et al. / Bioresource Technology 96 (2005) 897–906
substrate (by weight) was added to the UV-photolysis
system under nitrogen atmosphere, the dechlorination
rate slowed appreciably as compared to that under
nitrogen atmosphere alone (Fig. 3, Table 1). The first
order reaction rate constant for dechlorination of 1
decreased from 0.6 · 10�4 s�1 to 0.45 · 10�4 s�1. Theaddition of 2% hydrogen peroxide on substrate to the
UV-photolysis 2 under nitrogen atmosphere, the dechlo-
rination rate of 2 is the same with that under nitrogen
atmosphere along; the rate constant of 0.43 · 10�4 s�1
for both (Fig. 4, Table 1). However, in the UV-photoly-
sis of 3, the addition of 2% hydrogen peroxide on sub-
strate under nitrogen atmosphere resulted in slowing
down slightly the dechlorination rate; the rate constantdecreased from 1.8 · 10�4 s�1 to 1.65 · 10�4 s�1 (Fig. 5,
Table 1).
It is well established that the rate of UV-photolysis
for hydrogen peroxide to produce hydroxyl radicals
(HO�) in aqueous solution is, in general, pH dependent
and increases with increasing concentration of alkaline
solution (Eq. (1)) (Legrini et al., 1993). In addition,
hydrogen peroxide undergoes decomposition by a dis-mutation reaction with a maximum rate at the pH of
its pKa value, i.e., pH11.6 (Eq. (2)) (Legrini et al.,
1993). The hydroxyl radicals thus produced are readily
recombined back to hydrogen peroxide (Eq. (3)). More-
over, when an excess of hydrogen peroxide is used, hyd-
roxyl radicals will oxidize the excess hydrogen peroxides
Fig. 7. Possible reaction mechanisms dechlorination of 2,4,6-trichloropheno
under nitrogen atmosphere.
to produce hydroperoxyl radicals via abstraction of
hydrogen atoms (Eq. (4)).
H2O2 !hm2HO� ð1Þ
H2O2 þHOO� ! H2OþO2 þHO� ð2Þ
2HO� ! H2O2 ð3Þ
H2O2 þHO� ! H2OþHOO� ð4Þ
The hydroperoxyl radical (Reox potential,
E0 = 1.70V) was much less reactive as oxidant than hyd-
roxyl radical (Reox potential, E0 = 2.80V). In addition,the concentration of hydroperoxyl radical was control-
led by the pH of the reaction system. The rate constant
for dechlorination of chlorophenols decreased, in gen-
eral, with increasing concentration of hydrogen peroxide
(Table 1). Thus, the lower dechlorination rate constant
in the H2O2/UV-photolysis of 1 was attributable to the
presence of excess hydrogen peroxide (Fig. 3, Table 1).
In the homolytic cleavage of Ar–Cl bonds of 2,4,6-tri-chlorophenol (1) in the alkaline solution on irradiation
of 254nm photons in the presence of hydrogen peroxide,
the substrate was present in the reaction medium as the
corresponding phenoxide anion 1a. Thus, in addition to
the cleavage of Ar–Cl bonds, 1a would undergo single-
electron abstraction by hydroxyl radical (HO�) to give
2,4,6-trichlorophenoxyl radical (1d) that was resonating
l (1) in alkaline solution by H2O2/UV-photolysis with 254nm photons
y = 100e-0.2241x
R2 = 0.9472 y = 100e-0.2084x
R2 = 0.985
y = 100e-0.2346x
R2 = 0.9852
y = 100e-0.2083x
R2 = 0.9721
0
20
40
60
80
100
120
0 1 2
Reaction Time (min)
Org
anic
ally
Bou
nd C
hlor
ine
Con
tent
(Mol
% p
er O
rigi
nal)
3 4 5 6 7 8 9
Fig. 8. Dechlorination of 2,3,4,5-tetrachloropehnol (2) on ozone-
involved oxidation systems. With O3 alone: (-�-�-); with O3/
UV-photolysis: (-j-j-); with O3–H2O2: (-m-m-); with O3–H2O2/
UV-photolysis: (-d-d-). Initial pH: 10.34; temperature: ambient; O3
charge: 0.1mmol/min; H2O2 charge: 2% on substrate by weight; UV
source: 12W low pressure Hg lamp (254nm photons).
y = 100e-0.1634x
R2 = 0.9966
y = 100e-0.1672x
R2 = 0.9901
y = 100e-0.1675x
R = 0.98272
y = 100e-0.1772x
R2 = 0.99140
20
40
60
80
100
120
0 2 4 6 8 10 12 14Reaction Time (min)
Org
anic
ally
Bou
nd C
hlor
ine
Con
tent
(Mol
% p
er O
rigi
nal)
Fig. 9. Dechlorination of 4,5-dichloroguaiacol (3) on ozone-involved
oxidation systems. With O3 alone: (-�-�-); with O3/UV-photolysis:
(-j-j-); O3–H2O2: (-m-m-); O3–H2O2 /UV-photolysis: (-d-d-). Initial
pH: 10.34; temperature: ambient; O3 charge: 0.1mmol/min; H2O2
charge: 2% on substrate by weight; UV source: 12W low pressure Hg
lamp (254nm photons).
R. Wang et al. / Bioresource Technology 96 (2005) 897–906 903
among radical species 1e and 1f (Fig. 7). Since 1 was
symmetric with respect to C1–C4 axis in the aromatic
ring, the chance of having radical species 1e was twice
that of radical species 1f. Addition of hydroxyl radical
to C-2 of 1e and C-4 of 1f produced the corresponding
chlorohydrol intermediates 14 and 15, which undergob-elimination to give chloride anion and 4,6-dichloro-
o- and 2,6-dichloro-p-quinones (7 and 5), respectively
(Fig. 7). As shown in Fig. 6, the resulting quinones 5
and 7 would further undergo dechlorination to the cor-
responding hydroxyquinones 11 and 13, respectively.
The dechlorination rate for the H2O2/UV-photolysis
of 4,5-dichlorguaiacol (3) in alkaline solution under
nitrogen atmosphere with hydrogen peroxide charge of2% on substrate was slightly slower than that by N2/
photolysis. Conceivably, the slower dechlorination rate
was attributable to the fact that 3 has a methoxyl group
substituted ortho to the phenolic hydroxyl group, and a
chlorine atom substituted meta to the phenolic hydroxyl
group but para to the methoxyl group. Consequently,
the compound would undergo oxidation by hydro-
peroxyl radical to give 2-methoxy-5-chloro-p-quinone,5-hydroxy-2-methoxy-p-quinone and 4,5-dichloro-o-
quinone in the O2/UV- and H2O2/UV-photolyses, the
formation of which was analogous to the formation of
5, 11 and 7 from 1 in the O2/UV- and H2O2/UV-photo-
lyses of 1, respectively. In addition, the Ar–Cl bond of 3
at C-5 undergoes initially only homolysis to give the cor-
responding m-aryl radical species and chlorine radicals
(ClÆ) under the reaction condition. It follows that thenature of substituents and number of chlorine substitu-
ents in phenol affect appreciably the rate constant for
dechlorination of chlorophenemols.
3.4. UV-photolyses with ozone and combination of
ozone–hydrogen peroxide under aerial atmosphere,
and oxidation with ozone and combination of ozone–
hydrogen peroxide
Ozone is one of the strongest and yet environment be-
nign oxidants. It was, therefore, applied to the UV-
photolysis systems to see its effect on the UV-photolysis
of chlorophenols with 254nm photons. The lignin model
compounds 2 and 3 in 0.01M NaOH solution (pH10.34)
were treated with O3/UV- and O3–H2O2/UV-photolyses
with 254nm photons, and with ozone alone (ozonation)and combination of ozone and hydrogen peroxide as
reference. Although some differences have been ob-
served, the dechorination rate constants for 2 and 3 were
significantly increased in the O3/UV- and O3–H2O2/UV-
photolyses, as compared to the N2/UV photolysis of 2
and 3 (Figs. 8 and 9, Table 1).
In alkaline solution, ozone reacts with hydroxide
anions by transferring an oxyl anion radical (�O�), con-jugated base of hydroxyl radical (HO�), from the ozone
to the hydroxide anion to give superoxide (�O�2) and
hydroperoxyl (HO2�) radicals. Alternatively, this could
be accomplished when an oxygen atom was transferred
from the ozone to the hydroxide anion with a concomi-
tant single-electron transfer from the hydroxide anion to
the ozone (Eq. (5)) (Forni et al., 1982). The products,
hydroperoxyl radicals and superoxide, then react further
to give hydroperoxyl anion (HOO�) and molecular oxy-
gen (O2) (Eq. (6)). Since reaction rate constant for reac-tion 6 was much larger than that for reaction 5 (second
order reaction rate constant 8.7 · 107M�1 s�1 versus
48M�1 s�1), combination of these two reactions could
be simplified as an overall reaction (Eq. (7)). This
reaction was determined to be second order with the
904 R. Wang et al. / Bioresource Technology 96 (2005) 897–906
reaction rate constant of (40 ± 2) · 106M�1 s�1 (Tomi-
yasu et al., 1985; Grasso, 1987; Wang, 1993).
O3 þHO� ! HOO� þ �O–O� ð5Þ
HOO� þ �O–O� ! HOO� þO2 ð6Þ
O3 þHO� ! HOO� þO2 ð7ÞThe hydroperoxyl anion subsequently undergoes sin-
gle-electron-transferring oxidation by ozone to give
hydroperoxyl radical (HOO�) and ozone anion radical
(�O�3) with second order reaction rate constant of
2.2 · 106M�1 s�1 (Eq. (8)), which is the initiation reac-
tion (Tomiyasu et al., 1985; Grasso, 1987; Wang,1993). The resulting hydroperoxyl radical dissociates to
give its conjugated base, superoxide anion (�O�2) in alka-
line solution with equilibrium constant (ja) of 10�4.8 (Eq.
(9)). The superoxide anion then undergoes single-
electron-transferring oxidation by ozone to producing
ozone anion radical (�O�3) and molecular oxygen with
second reaction rate constant of 1.6 · 109M�1 s�1 (Eq.
(10)) (Sehested et al., 1983). The ozone anion radicalundergoes hydrolysis to hydroxyl radical (HO�), molecu-
lar oxygen (O2) and hydroxide anion (HO�) with second
order reaction rate of approximately 30M�1 s�1 (Eq.
(11)) (Tomiyasu et al., 1985; Grasso, 1987; Wang,
1993). In addition, the cross radical combination be-
tween the ozone anion radical and hydroxyl radical, fol-
lowed by homolytic cleavage of the �O–O–O–O–H
intermediate produces supper oxide anion and hydrope-roxyl radical with second reaction rate constant of
6 · 109M�1 s�1 (Eq. (12)). Alternatively the ozone anion
radical undergoes oxidation by hydroxyl radical to pro-
duce ozone and hydroxide anion with second reaction
rate constant of 2.5 · 109M�1 s�1 (Eq. (13)) which re-
turns to the initiation reaction state (Eq. (8)) after series
of reactions.
HOO� þO3 ! HOO� þ �O�3 ð8Þ
HOO� þHO��
�O–O� þH2O ð9Þ�O–O� þO3 ! �O�
3 þO2 ð10Þ
�O�3 þH2O ! HO� þO2 þHO� ð11Þ
�O�3 þHO� ! �O–O� þHOO� ð12Þ
�O�3 þHO� ! O3 þHO� ð13ÞThus, the ozone dissolved in alkaline solution is a
rather complex chemical system that contains several
reactive chemical species. Conceivably, these chemicalspecies contribute to degradation of chlorophenols in
alkaline solution saturated with ozone although it is
not well established the effectiveness of ozone molecules
under the reaction condition.
On the basis of numerous investigations (Legrini
et al., 1993), a two step process was proposed to involve
the UV light-induced homolysis of ozone in aqueous
solution. It has been postulated that ozone in aqueous
solution undergoes homolysis on irradiation of UV light
with wavelength smaller than 310nm to give molecular
oxygen and O(1D) species (Eq. (14)). The latter then re-
acts with water to produce hydroxyl radicals (HO�) (Eq.(15)) (Legrini et al., 1993). However, it has been ob-
served that UV-photolysis of ozone dissolved in water
leads to the formation of hydrogen peroxide (Eq. (16))
in a sequence of reactions, where hydroxyl radicals,
if formed at all, can not escape from the solvent cage
(Legrini et al., 1993).
O3 !hm<310 nmO2 þOð1DÞ ð14Þ
Oð1DÞ þH2O ! HO� þHO� ð15Þ
O3 þH2O!hm ! H2O2 þO2 ð16Þ
Conceivably, the hydrogen peroxide produced in the
O3/UV-photolysis under aerial atmosphere undergoes
dissociation to give superoxide anion. The hydroperoxyl
anion was subsequently oxidized by ozone (Eq. (8)) to
give hydroperoxyl radical (HOO�) and ozone anion radi-
cal (�O�3), which initiate reactions 9–13. Therefore, the
reactive chemical species in the O3/UV-photolysis in
alkaline solution were almost the same with those with
ozone dissolved in water, except for the generation of
hydroxyl radical by UV-photolysis of ozone (Eqs. (11),
(14) and (15)). Thus, addition of hydrogen peroxide to
the O3/UV-photolysis would not promote the dechlorin-
ation of chlorinated phenols appreciably, which was in
good agreement with the kinetics of the O3/UV- andO3–H2O2/UV-photolyses of 2 and 3 (Figs. 8 and 9,
Table 1).
It is noteworthy that the reactions of chlorophenols
with ozone and the chemical species derived from ozone
dissolved in alkaline solution are mostly electrophilic
reactions that prefer phenols substituted with electron-
attracting groups. Although aliphatic hydroxyl and
methoxyl groups are electron-attracting groups, botharomatic hydroxyl and methoxyl groups are strong elec-
tron-releasing groups in term of inductive effect. This re-
sults in activating the corresponding aromatic ring. In
addition, the resonance effect of their lone electron-pairs
result in electron-rich centers at the carbon atoms ortho
and para to these groups, which readily undergo electro-
philic attack by ozone and most of the chemical species
derived from ozone in alkaline solution. In contrast,aromatic halogen is an electron-attracting group and
the resulting inductive effect deactivates the ring. How-
ever, resonance of lone electron pairs in the aromatic
halogen also establishes electron-rich centers at the car-
bon atoms ortho and para to the halogen group. Thus,
the aromatic ring with more chlorine substituents is
likely to undergo less electrophilic attack by ozone and
R. Wang et al. / Bioresource Technology 96 (2005) 897–906 905
the chemical species derived from ozone because of the
greater deactivation of the aromatic ring. Consequently,
4,5-dichlorguiacohol (3) should be easier to undergo
oxidative degradation by ozone with concomitant
dechlorination than 2,3,4,5-tetrachlorophenol (2). How-
ever, the opposite is true (Figs. 8 and 9, Table 1). Whenalkaline solutions of 2 and 3 were treated with ozone
alone, the dechlorination rate of 2 was much faster than
that of 3, the rate constant of 3.74 · 10�4 s�1 versus
2.72 · 10�4 s�1 (Table 1). Conceivably, 3 is susceptible
to electrophilic attack by ozone and the chemical species
derived from ozone at C-1 and C-2 leading to an oxida-
tive ring cleavage between these two carbons with oxy-
gen-containing functional groups because of the higherelectron density in these carbon atoms (Kratzl et al.,
1976). A ring cleavage of this nature will not convert
organically bound chlorine (OCl) directly to chloride
anion (Cl�). However, the resulting a,b-unsaturatedcarbonyl intermediates containing a b-chlorine sub-
stituent could undergo further nucleophilic attack by
hydroxide anion, followed by b-elimination of Cl�. In
contrast, 2 is less susceptible to the oxidative ringcleavage than the aromatic ring of 3 does because the
aromatic ring of 2 is deactivated more by chlorine-sub-
stituents. However, when 2 undergoes oxidative ring
cleavage, it produces immediately Cl� from OCl. As a
result, the dechlorination rate of 3 is slower than that
of 2. Nevertheless, over 85% of OCl could be removed
from these chlorophenols in less than reaction time of
15min by treatment with ozone alone. When 2 wastreated with the O3/UV- and O3–H2O2/UV-photolysis
systems, the dechlorination rate constant for the
O3/UV-photolysis was slightly decreased as compared
to the treatment with O3 alone, 3.47 · 10�3 s�1 vs
3.74 · 10�3 s�1 (Fig. 8, Table 1). In contrast, the dechlo-
rination rate constant for the O3–H2O2/UV-photolysis
was slightly increased as compared to the treatment with
the combination of O3 and H2O2, 3.91 · 10�3 s�1 vs3.74 · 10�3 s�1 (Fig. 8, Table 1). However, the dechlo-
rination rate constant for the O3/UV-photolysis was
the same with that in the treatment of 2 with the combi-
nation of O3 and H2O2. When 3 was treated by O3/UV-
and O3–H2O2/UV-photolysis systems, no appreciable
differences in the dechlorination rates were observed;
dechlorination rate constant for both is 2.8 · 10�3 s�1
(Fig. 9, Table 1). These results clearly indicate that deg-radation reactions by chemical species derived from
ozone and hydrogen peroxide in alkaline solution are
dominant reactions in the dechlorination of 2 and 3 by
the O3/UV- and O3–H2O2/UV-photolysis systems.
4. Conclusions
On the basis of kinetic data, the dechlorination of
2,4,6-trichlorophenol (1), 2,3,4,5-tetrachlorophenol (2)
and 4.5-dichloroguaiacol (3) in alkaline solution by
N2/UV-, O2/UV-H2O2/UV-, O3/UV- and O3–H2O2/
UV-photolyses is first order reaction with respect to
the organically bound chlorine in the substrate. The
dechlorination of 1–3 in alkaline solution by O2/UV-
and H2O2/UV-photolyses is less effective than the corre-sponding N2/UV-photolysis of 1–3, except for the O2/
UV-photolysis of 1 and H2O2/UV-photolysis of 2. Gua-
iacol-type chlorophenols are more likely to undergo
dechlorination than non-guaiacol type chlorophenols
by N2/UV-, O2/UV- and H2O2/UV-photolyses. In addi-
tion, the efficiency for the dechlorination of 1–3 by N2/
UV-, O2/UV- and H2O2/UV-photolyses seems to be
dependent upon the inductive and resonance effects ofsubstituents as well as number and position of chlorine
substituent in the aromatic ring of the compounds.
Introduction of ozone and combination ozone and
hydrogen peroxide into the UV-photolysis system result
in appreciable improvement in dechlorination of 2 and
3, which were effectively degraded. Up to �40% of the
total organically bound chlorine in these compounds
was converted into chloride ion within reaction time of5min. However, the dechlorination of 2 by treatment
with O3 alone is slightly more effective than the corre-
sponding the O3/UV-photlysis, whereas the dechlorina-
tion of 2 by treatment with the combination of O3 and
H2O2 is slightly less effective than the corresponding
O3–H2O2/UV-photolysis. In contrast, the dechlorination
of 3 on treatment with O3 alone is slightly less effective
than the corresponding the O3/UV-photolysis, whereasthe dechlorination of 3 on treatment with the combina-
tion of O3 and H2O2 is slightly more effective than the
corresponding the O3–H2O2/UV-photolysis. Thus, in
the dechlorination of 2 and 3, chemical species derived
from ozone and hydrogen peroxide in alkaline solution
are dominant reactions in the O3/UV- and O3–H2O2/
UV-photolysis systems.
Acknowledgements
This project is supported by the USDA competitive
research grant under cooperative agreement no. 88-
33521-4084, for which the authors are thankful. The
authors are also grateful to Mead-Westvaco Corpora-
tion for supplying the E-1 effluent for this study.
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