RSC Advances
View Article Online
Published on 05 August 2014. Downloaded by University of Birmingham on 26/08/2014 06:04:41.
REVIEW
Cite this: RSC Adv., 2014, 4, 37003
View Journal | View Issue
Principles and mechanisms of photocatalytic dye
degradation on TiO2 based photocatalysts: a
comparative overview
Anila Ajmal,a Imran Majeed,b Riffat Naseem Malik,a Hicham Idrissc
and Muhammad Amtiaz Nadeem*ac
The total annual production of synthetic dye is more than 7 105 tons. Annually, through only textile waste
effluents, around one thousand tons of non-biodegradable textile dyes are discharged into natural streams
and water bodies. Therefore, with growing environmental concerns and environmental awareness there is a
need for the removal of dyes from local and industrial water effluents with a cost effective technology. In
general, these dyes have been found to be resistant to biological as well as physical treatment technologies.
In this regard, heterogeneous advanced oxidation processes (AOPs), involving photo-catalyzed degradation
of dyes using semiconductor nanoparticles is considered as an efficient cure for dye pollution. In the last
two decades TiO2 has received considerable interest because of its high potential as a photocatalyst to
degrade a wide range of organic material including dyes. This review starts with (i) a brief overview on
dye pollution, dye classification and dye decolourization/degradation strategies; (ii) focuses on the
Received 4th July 2014
Accepted 4th August 2014
mechanisms involved in comparatively well understood TiO2 photocatalysts and (iii) discusses recent
advancements to enhance TiO2 photocatalytic efficiency by (a) doping with metals, non-metals,
transition metals, noble metals and lanthanide ions, (b) structural modifications of TiO2 and (c)
DOI: 10.1039/c4ra06658h
immobilization of TiO2 by using various supports to make it a flexible and cost-effective commercial dye
www.rsc.org/advances
treatment technology.
Dye pollution-an overview
Dyes play a vital role in various branches of the dyeing and
textile industries. Over 100 000 commercially available
synthetic dyes are the most frequently used dyes in such
industries. These dyes are usually derived from two main
sources i.e. coal tar and petroleum intermediates with a total
annual production of more than 7 105 tons.5–7 Annually,
through textile waste effluents, around 15% (one thousand
Department of Environmental Sciences, Quaid-i-Azam University, Islamabad 4200,
Pakistan. E-mail: NadeemMI@SABIC.com
a
b
c
Department of Chemistry, Quaid-i-Azam University, Islamabad 4200, Pakistan
tons) of these non-biodegradable textile dyes are discharged
into natural streams and water bodies.1–4,8,9 Typically, on an
average for every kilogram of cloth, being processed in dyeing
and nishing plants, about 120–280 L of water is being
consumed.10
Konstantinou and Albanis11 reported that industrial dye
stuffs and textile dyes constitute one of the largest groups of
toxic organic compounds. According to an estimate made by
World Bank, nearly 17–20% water pollution has the major
contributors related to textile nishing and dyeing industries.
According to a study by Kant, out of major identied wastewater
toxic chemicals, 72 chemicals were solely released by the textile
dyeing and nearly 30 of such chemicals were not treatable.12 In
CRI-KAUST, Saudi Basic Industries Corporation, Thuwal, Saudi Arabia
Anila Ajmal has recently completed her M.Phil in Environmental
Remediation from Quaid-i-Azam University, Islamabad, Pakistan.
She has recently completed her M.Phil thesis project that focuses
photocatalytic treatment of dye contaminated wastewater. She
obtained her BS honors (2010) in Environmental Sciences from
Lahore College for Women University, Lahore, Pakistan. Her main
research interests include applications of photocatalytic techniques for the remediation of environmental contaminants.
This journal is © The Royal Society of Chemistry 2014
Imran Majeed is currently doing his Ph.D at Department of
Chemistry, Quaid-i-Azam University Islamabad, Paksiatan. His
Ph.D project is about hydrogen production from renewables using
visible light active TiO2 based photocatalysts. He completed
Masters (2005) in Applied Chemistry from University of Engineering and Technology, Lahore, Pakistan and M.Phil (2008) in
Analytical/Inorganic Chemistry from the same University. Before
starting his Ph.D, he was been working as Senior Scientist in
Pakistan Atomic Energy Commission, Islamabad, Pakistan.
RSC Adv., 2014, 4, 37003–37026 | 37003
View Article Online
Published on 05 August 2014. Downloaded by University of Birmingham on 26/08/2014 06:04:41.
RSC Advances
1974, Ecological and Toxicological Association of the Dyestuffs
Manufacturing Industry (ETAD) was formed with an aims to
protect consumers by preventing and reducing environmental
damages by fully cooperating with government over the
concerns related to the toxicological impact of their own products.13 In an ETAD survey, of all 4000 tested dyes, 90% dyes were
found to be having their LD50 values greater than 2 103 mg
kg 1. Among all tested dyes diazo, direct and basic dyes showed
the highest rates of toxicity.14
Bright coloured dyes such as reactive and acid dyes are water
soluble and the most problematic dyes to remove.15 Conventional and municipal aerobic treatment systems have been
proved to be ineffective on both type of dyes.16,17 Compared to
other types of dyes, reactive dyes are least taken up by the fabric
during dyeing process, implying that the remaining quantity of
dye is directly lost into the wastewater.18 Leena and Raj19
reported that reactive dye effluent possess the ability to remain
stable and unaffected in environment for several years i.e.
hydrolyzed reactive blue 19 has a half-life of about 46 years.
Dispersed dyes do not ionize in an aqueous medium enhancing
Riffat Naseem Malik is currently an Associate Professor as well as
Chairperson of Department of Environmental Sciences, Quaid-iAzam University Islamabad, Pakistan. Before this, she worked as
Post-Doctoral Research Fellow (2001–2003) at Lancaster Environmental Centre, Lancaster University, UK. She has completed her
Ph.D in Environmental Biology from The Reading University,
Reading, UK. She had received Research Fellowship from Department of Geography, University of Turku, Finland aer completing
her M.Phil and M.Sc from Quaid-i-Azam University, Islamabad,
Pakistan. She is the author and co-author of more than 90 scientic
publications.
Hicham Idriss is currently working at CRI-KAUST, Saudi Basic
Industries Corporation, Thuwal, Saudi Arabia as Chief Scientist.
Formerly, he worked as Aberdeen Energy Futures Chair and
Professor of Chemistry at the University of Aberdeen and Robert
Gordon University, UK from 2008 to 2010. He is also Adjunct
Professor at the Department of Chemical Engineering, Louisiana
State University in the USA. Prior to 2008 he was Associate
Professor at the Department of Chemistry, the University of
Auckland in New Zealand where he worked for 13 years. He served
as a member of the New Zealand National Energy Panel who
delivered the 2020 Energy report to the New Zealand Government
in 2008. He has obtained his B.Sc (1984), M.Sc (1985), Ph.D (1987)
and habilitation (1997) from the University of Strasbourg in
France and has postdoctoral and research associate positions at
the University of Delaware and University of Illinois, Urbana
(USA). He is the author and co-author of over 140 scientic papers
and has served/is serving at the editorial board of scientic journals including Applied Catalysis A, Catalysis Today and Catalysis
Survey from Asia. His main interest in surface science and catalysis
is on metal oxides and their interface with transition metals at the
fundamental and applied levels.
37004 | RSC Adv., 2014, 4, 37003–37026
Review
their ability to bioaccumulate in aquatic living organisms.20
Currently concerns related to the dye effluents are arising as
many dyes are synthesized by known carcinogens such as
aromatic compounds and benzidine.20
Chung et al.21 have illustrated the dye reduction in the
intestinal environment, that resulted into the formation of toxic
amines. Moreover, azo dyes are readily reduced into the
aromatic amines that are potentially hazardous as a result of
anaerobic treatment conditions.22–25
In addition to dye pollution, in textile industries processing
prior to dying procedure such as mercerization, scouring, sizing
and bleaching results into the production of bleaching as well
as scouring agents. However, amongst all of above mentioned
concerns, colour removal from wastewater is the most complex
and difficult task.18 Dyes are usually the rst contaminant to be
recognized in industrial wastewater due to their high visibility
even in minute concentrations (<1 ppm).26 These coloured
wastewaters are a considerable source of eutrophication as well
as non-aesthetic pollution that can produce dangerous byproducts by further oxidation, hydrolysis, or other chemical
reactions taking place in the wastewater phase. Apart from the
toxic effects of dyes in wastewater streams, presence of dyes can
cause reduced light penetration resulting in reduced photosynthetic activity thus making oxygen unavailable for biodegradation of microorganism in the water.27
Apart from the textile industry, leather tanning industry,28
paper industry,29 food industry,30 hair colourings,31 photoelectrochemical cells32 and light-harvesting arrays33,34 also
contribute towards the presence of dyes in wastewater. Majority
of dyes used in various industries are toxic and carcinogenic
thus posing a serious hazard to humans as well as to marine
ecosystem.35 Therefore, the impact of dyes released into the
environment have been studied extensively in last few years.36,37
Muhammad Amtiaz Nadeem is currently an Assistant professor at
Quaid-i-Azam University Islamabad. He completed Masters (2003)
in Chemistry from University of the Punjab, Lahore, Pakistan and
M.Phil in Analytical/Inorganic Chemistry (2006) from Quaid-iAzam University Islamabad, Pakistan. He joined Prof. Hicham
Idriss group based at University of Auckland as a Ph.D student in
2008 and in 2009 moved with him at the Energy Future Center in
Aberdeen, UK, to complete his Ph.D in 2012. His Ph.D thesis has
been placed in Dean, Faculty of Natural Sciences, University of
Auckland theses excellence list. His thesis was also nominated for
University of Auckland best thesis award for 2012. His main
interest in surface science and catalysis is on metal oxides and
their interface with transition metals at the fundamental and
applied levels.
This journal is © The Royal Society of Chemistry 2014
View Article Online
Review
This paper presents an overview of the recent research
improvements targeting the degradation of various dyes by
using TiO2 as a potential photocatalyst.
Published on 05 August 2014. Downloaded by University of Birmingham on 26/08/2014 06:04:41.
Dye classification
Dyes usually have many structural varieties and their complete
classication with respect to one parameter is very difficult and
of no use from practical understanding point of view. However,
dyes are generally divided into different groups and classes
depending on their source, general dye structure and the ber
type with which they are most compatible as shown in the Fig. 1.
Among major dye categories, azo dyes are the largest group
of colourants and over 50% of all the dyes used in industries are
azoic dyes. Azo dyes are characterized by double bond of nitrogen
(–N]N–), where at least one of the nitrogen atom is attached to an
aromatic group (rings of naphthalene or benzene). Moreover, they
have amphoteric properties due to the presence of additional
carboxyl, hydroxyl, amino or sulfoxyl functional groups. Azo
dyes can behave anionic (deprotonation at the acidic group),
cationic (protonated at the amino group) or non-ionic
depending upon the pH of the medium.38 Most notable azo
dyes are: acid dyes, basic dyes (cationic dyes), direct dyes
(substantive dyes), disperse dyes (non-ionic dyes), reactive dyes,
vat dyes and sulfur dyes.39 Dyes based on general structure can
also be classied as anionic, non-ionic and cationic dyes. The
anionic dyes mainly include direct acidic and reactive dyes.26
Major nonionic dyes include; disperse dyes which does not
ionizes in the aqueous environment and the major cationic dyes
include basic and disperse dyes.38
Acidic dyes are named so as they are normally applied to the
nitrogenous bers or fabrics in inorganic or organic acid solutions. Basic dyes give cations in the solution which are generally
applied to acrylic and modacrylic bers. Direct dyes are applied
in aqueous bath containing ionic salts and electrolytes that
bond to bers/fabrics by electrostatics forces.40,41 Disperse dyes
have low solubility in water, but they can interact with the
Fig. 1 Flow chart indicating dye classification on the basis of dye
chemical constitution and its application.
This journal is © The Royal Society of Chemistry 2014
RSC Advances
polyester chains by forming dispersed particles.42 The wash
fastness with disperse dyes varies with the type of bers being
used for dyeing purpose i.e. poor on acetate, excellent on polyester.38 Reactive dyes are primarily utilized on cellulosic bers,
but occasionally on protein bers and nylon as well forming
covalent bond with the appropriate textile functionality.43 Sulfur
dyes are used on cellulosic bers to produce dull shades such as
navy, black and brown. They have excellent fastness in most
areas, but fades off when exposed to chlorine. Vat dyes that
works with a special chemistry having excellent fastness in all
areas and especially on exposure to chlorine and bleach.44–46
Further characteristics of these dyes are summarized in Table 1.
Dye treatment strategies
Apart from their physically unpleasant nature and toxicity, ever
increasing massive production rate of dyes due to increasing
industrialization have led to the necessity of effective treatment.47,48 Therefore, in order to treat such obvious and challenging effluents, a wide range of technologies have been tested
to reduce their potential magnied impacts on environment.
Traditional physical techniques such as activated carbon,
adsorption, reverse osmosis, ultraltration can be used for dye
removal. However, these processes simply transfer the pollutants from one to another medium causing secondary pollution.
This generally requires further treatment of solid-wastes and
regeneration of the adsorbent, which adds more cost to the
process. Chemical process such as chlorination, ozonation,49
adsorption on organic or inorganic matrices, precipitation,
chemical oxidation processes,50 advanced oxidation processes
such as Fenton and photo-Fenton catalytic reactions,51 H2O2/UV
processes52 and photodegradation through photocatalysis are
also commonly being used for the synthetic dye removal.53
However, toxic unstable metabolites as a result of most of these
processes54 imparts adverse effects on animal and human
health.55
Biological processes involving microbiological or enzymatic
decomposition56 and biodegradation have also been used for
dye removal from wastewaters. Moutaouakkil et al.57 isolated
Azoreductase enzyme from Enterobacter agglomerans having
ability to grow fast on methyl red dye under aerobic condition by
catalyzing reductive cleavage of azo bonds. Anaerobic conditions also facilitates58 the azo bond rupture leading to the colour
disappearance but result in incomplete mineralization of toxic
and carcinogenic by-products.59 However, it has been found that
these conventional biological treatment processes are ineffective for synthetic dyes having recalcitrant nature.60,61 In recent
years, a broad range of synthetic dyes have been extensively
studied to develop a more promising technology based on
advanced oxidation process (AOPs) that has the ability to oxidize
contaminants quickly and non-selectively.50,62,63 AOPs rely on in
situ production of highly reactive hydroxyl radicals (OH_) which
can virtually oxidize any compound present in the water matrix,
oen at a diffusion controlled reaction speed. These radicals are
produced with the help of one or more primary oxidants (e.g.
ozone, hydrogen peroxide, oxygen) and/or energy sources (e.g.
ultraviolet light) or catalysts (e.g. titanium dioxide).64,65 This
RSC Adv., 2014, 4, 37003–37026 | 37005
View Article Online
RSC Advances
Table 1
Types and characteristic classification of azo dyes
Dye class
Characteristics
Fiber
Dye xation (%)
Pollutant
Acidic
Water-soluble anionic
compounds
Water-soluble, applied in
weakly acidic dye baths, very
bright dyes
Water-soluble, anionic
compounds, applied without
mordant
Wool, nylon, cotton blends,
acrylic and protein bers
Acrylic, cationic, polyester,
nylon, cellulosic, and
protein bers
Cotton, rayon and other
cellulosic bers
80–93
Colour; organic acids;
unxed dyes
NA
Dispersive
Insoluble in water
Polyester, acetate,
modacrylic, nylon, polyester,
triacetate and olen bers
80–92
Reactive
Water-soluble, anionic
compounds, largest dye
class
Organic compounds
containing sulfur or sodium
sulde
Oldest dyes, chemically
complex, water-insoluble
Cotton, cellulosic and wool
bers
60–90
Cotton and other cellulosic
bers
60–70
Cotton, wool and other
cellulosic bers
60–70
Basic
Direct
Published on 05 August 2014. Downloaded by University of Birmingham on 26/08/2014 06:04:41.
Review
Sulphur
Vat
review focuses on mechanistic and practical aspects of dye
degradation by TiO2 based photocatalysts.
Photocatalytic dye treatment
Heterogeneous photocatalysis has proved to be as an efficient
tool for degrading both atmospheric and aquatic organic
contaminants.66 It uses the sunlight in the presence of a semiconductor photocatalyst to accelerate the remediation of environmental contaminants and destruction of highly toxic
molecules.67,68 The type of the radiation used depends on the
type of catalyst i.e. pure TiO2 works under UV light (370–415
nm). Visible light can also be used for the excitation purpose but
due to unavailability of proper catalyst and other contributing
factor, it has been considered as less effective source for irradiation. Generally speaking, nal products of TiO2 photocatalysis have not been reported properly, which oen makes
evaluation of the photocatalysis difficult. The reactions of dye
molecules on TiO2 photocatalysts are oen confusing, and
could be classied into the following categories according to the
photocatalysis products. (1) Photodecolourization69–73 involves
simple photooxidation or photoreduction where dyes can
return to the original form by either corresponding back
reduction or back oxidation, respectively. (2) Photodegradation74–79 involves dye decomposition to some stable
products. It is the most widely used name for photocatalytic dye
treatment. (3) Photomineralization80–84 is regarded as complete
decomposition to CO2, H2O, N2, NO3 , NO2 etc. The goal of
ideal photocatalysis should be mineralization. (4) Photodecomposition76,77 could imply both photodegradation and
mineralization differently, depending also on the researchers.
However, it rarely involves decolourization. Hereaer in this
37006 | RSC Adv., 2014, 4, 37003–37026
97 and 98
70–95
Colour; salts; unxed dye;
cationic xing agents;
surfactant; defoamer;
levelling and retarding
agents; nish; diluents
Colour; organic acids;
carriers; levelling agents;
phosphates; defoamers;
lubricants; dispersants;
delustrants; diluents
Colour; salt; alkali; unxed
dye; surfactants; defoamer;
diluents; nish
Colour; alkali; oxidizing
agent; reducing agent;
unxed dye
Colour; alkali; oxidizing
agents; reducing agents
review care will be taken to use these terminologies as precisely
as possible.
In order to assess the degree of dye photodegradation achieved during the treatment, generally formation of CO2 and
inorganic ions is determined.81,82,85–88 However, it is impossible
to measure the exact concentration of these ions in case of real
wastewaters. In such cases the determination of total organic
carbon (TOC) or the measurement of the chemical oxygen
demand (COD) or the biological oxygen demand (BOD) is used
to monitor extent of dye mineralization.82,83,86,89–92 In general, at
lower dye concentration and for compounds which do not form
stable intermediates, complete mineralization proceed with
similar half-lives for parent dye and the intermediates but at
higher concentration intermediates mineralization is slower
than the degradation of the parent dye. To date most azo dyes
have been found to undergo complete mineralization except
triazine containing dyes.81–84,90 The later does not undergo
complete mineralization due to high stability of triazine
nucleus and the stable cyanuric acid intermediates.93 However,
fortunately these intermediates are not toxic.80,91,92 Usually COD
or TOC values decrease with irradiation time whereas the
amount of NH4+, Cl , SO42 and NO3 ions increase.81,91,94
For chlorinated dye molecules, Cl ions are the rst of the
ions which appear during photocatalytic degradation.90,92,95 This
could be interesting in photocatalytic biological treatment
which is generally not efficient for chlorinated compounds.
Nitrogen is mineralized into NH4+, NO3 and N2 depending
upon initial oxidation oxidation state of nitrogen, the substrate
structure and irradiation time.96,97 The total amount of nitrogencontaining ions present in the solution at the end of the
experiments is usually lower than that expected from stoichiometry indicating that N-containing species remain adsorbed
This journal is © The Royal Society of Chemistry 2014
View Article Online
Published on 05 August 2014. Downloaded by University of Birmingham on 26/08/2014 06:04:41.
Review
in the photocatalyst surface or most probably, that signicant
quantities of N2 and/or NH3 have been produced and transferred to the gas-phase.81,83,90
The dyes containing sulfur atoms are mainly mineralized
into sulfate ions stoichiometrically.92,95 Non-stoichiometric
formation of sulphate ions is usually explained by a strong
SO4 adsorption on the photocatalyst surface which could
partially inhibit the reaction rate.81,98,99 Generally, it is found
that nitrate anions have little effect on the kinetics of reaction
whereas sulfate, chloride and phosphate ions, especially at
concentrations of greater than 10 3 mol dm 3, can reduce the
rate by 20–70% due to the competitive adsorption at the photoactivated reaction sites.98
TiO2 as dye treatment photocatalyst
Among various types of photocatalysts, titanium dioxide (TiO2)
assisted photocatalytic oxidation has received much attention
the last few years due to its non-toxicity, strong oxidizing power
and long-term photostability.100 Titanium dioxide (TiO2) is a
white powder semiconductor having a wide band gap of 3.0–3.2
eV.101–103 It can be excited by UV light with a wavelength below
ca. 415 nm (in its rutile form). However, the use of TiO2 is
limited as only about 3–4% of the solar spectrum falls within UV
range.102,104–106 In general, there are three types of titanium
dioxide i.e. anatase, rutile and brookite. In general TiO2 nanoparticles are widely available commercially or can be easily
prepared using sol gel method. Typically, anatase phase is oen
found having particle size equal to 10 nm or less with a band
gap of 3.2 eV corresponding to a UV wavelength of 385 nm.107
Comparatively, though some exceptions exists, rutile phase
generally exists having particle size in the order of 50 nm or
so.108 Moreover, rutile has a smaller band gap of 3.0 eV with
excitation wavelengths extending to visible 410 nm range.
Thermodynamics dictates that heating the anatase phase
results in gradual phase transformation of anatase to rutile and
therefore depending on the method of preparation mix phase
anatase-rutile can be easily prepared or purchased. For
example, some commercially available TiO2 that is a mixture of
two phases, 80% anatase and 20% rutile, and has usually a BET
area of 50 m2 g 1 has widely been studied.109
Most of the studies have been carried out with anatase phase
due to its high photocatalytic efficiency and adsorption affinity
for the organic compounds as compared to the rutile
phase.110,111 Shiga et al.112 using nanocrystalline lm electrodes
of TiO2 for photoelectrochemical activities showed that the
anatase has a higher photoactivity than rutile phase at a longer
wavelength. This is due to the fact that anatase phase due to its
greater hole trapping ability (about 10-fold) exhibits lower
recombination rates compared to rutile type.113,114 Therefore,
anatase is generally regarded as photochemically more active
phase of TiO2 due to these combined effect.107 Moreover,
recently developed various forms of TiO2, such as TiO2 powders,
TiO2 lm,115 supported TiO2,116,117 TiO2 nanotubes118 and doped
TiO2119,120 have been evaluated through degradation of dyes and
phenolic compounds. Such studies demonstrated the higher
This journal is © The Royal Society of Chemistry 2014
RSC Advances
efficiency of various forms of TiO2 used for removal of dyes and
phenolic compounds from aqueous solutions.121
Basic principles and mechanism for
photocatalyzed dye degradation
Indirect dye degradation mechanism
The indirect heterogeneous photocatalytic oxidation mechanism using semiconducting materials can be summarized as
follows.122,123
a. Photoexcitation. Photocatalytic reaction is initiated
when a photoelectron is promoted from the lled valence band
of a semiconductor photocatalyst i.e. TiO2 to the empty
conduction band as a result of irradiation. The absorbed
photon has energy (hn) either equal or greater than the band gap
of the semiconductor photocatalyst. The excitation process
leaves behind a hole in the valence band (hVB+). Thus as a net
result, electron and hole pair (e /h+) is generated as indicated
by the eqn (1) below.
TiO2 + hn(UV) / TiO2(e (CB) + h+(VB))
(1)
b. Ionization of water. The photogenerated holes at the
valence band then react with water to produce OH_ radical.
H2O(ads) + h+(VB) / OH_(ads) + H+(ads)
(2)
The HO_ radical formed on the irradiated semiconductor
surface are extremely powerful oxidizing agent. It attacks
adsorbed organic molecules or those that are very close to the
catalyst surface non-selectively, causing them to mineralize to
an extent depending upon their structure and stability level. It
does not only easily attack organic pollutants but can also attack
microorganisms for their enhanced decontamination.124
c. Oxygen ionosorption. While the photogenerated hole
(hVB+) reacts with surface bound water or OH to produce the
hydroxyl radical, electron in the conduction (eCB ) is taken up
by the oxygen in order to generate anionic superoxide radical
(O2 ).
O2 + e (CB) / O2 _(ads)
(3)
This superoxide ion may not only take part in the further
oxidation process but also prevents the electron-hole recombination, thus maintaining electron neutrality within the TiO2
molecule.
d. Protonation of superoxide. The superoxide (O2 _)
produced gets protonated forming hydroperoxyl radical (HO2_)
and then subsequently H2O2 which further dissociates into
highly reactive hydroxyl radicals (OH_).
O2 _(ads) + H+ % HOO_(ads)
(4)
2HOO_(ads) / H2O2(ads) + O2
(5)
H2O2(ads) / 2OH_(ads)
(6)
RSC Adv., 2014, 4, 37003–37026 | 37007
View Article Online
Published on 05 August 2014. Downloaded by University of Birmingham on 26/08/2014 06:04:41.
RSC Advances
Review
Dye + OH_ / CO2 + H2O(dye intermediates)
(7)
Dye + h+(VB) / oxidation products
(8)
Dye + e (CB) / reduction products
(9)
Both oxidation and reduction processes commonly take
place on the surface of the photoexcited semiconductor photocatalyst. The complete process has been represented by the
Fig. 2.
Direct mechanism for dye degradation
Owing to their ability to easily absorb some of visible light,
another mechanism of photocatalytic dye degradation can also
occur under visible light. This mechanism involves the dye
excitation under visible light photon (l > 400 nm) from the
ground state (Dye) to the triplet excited state (Dye*). This excited
state dye species is further converted into a semi-oxidized radial
cation (Dye+_) by an electron injection into the conduction band
of TiO2.125 Due to reaction between these trapped electrons and
dissolved oxygen in the system superoxide radical anions (O2 _)
are formed which in turn result into hydroxyl radicals (OH_)
formation. These OH_ radicals are mainly responsible for the
oxidation of the organic compounds represented by the equations and Fig. 3 below.126–128
Dye + hn / dye*
(10)
Dye* + TiO2 / dye+ + TiO2
(11)
According to many studies, indirect mechanism is generally
prevalent over direct mechanism and its contribution to the dye
degradation is much more pronounced than the visible light
initiated mechanism. The latter is believed to be a far slower
reaction compared to indirect mechanism.126,129
Factors affecting photocatalytic dye
degradation
Effect of pH
The pH is one of the signicant parameters for the photocatalytic dye degradation as it can inuence dye reaction rates
in multiple ways as explained here on. It can inuence dye
adsorption onto the semiconductor surface121 as catalyst surface
charge depends on the pH of a given solution. Zhu et al.130
Fig. 2
Pictorial representation of indirect dye degradation process.24
37008 | RSC Adv., 2014, 4, 37003–37026
Fig. 3
Pictorial representation of direct dye degradation process.
demonstrated that pH effect is related to the surface-charge
properties of the photocatalysts, and could be explained on
the basis of point of zero charge (PZC). The point of zero charge
for TiO2 particles is pHpzc ¼ 6.8.3 At a pH values lower than
pHpzc (pH < 6.8) or at acidic solution, the surface of the catalyst
gets positively charged and vice versa131,132 according to the eqn
(12) and (13) given below.
TiOH(Surface) + H+ / TiOH2(surface)+
(12)
TiOH(Surface) + OH / TiO(Surface) + H2O
(13)
When the pH is lower than the PZC value the adsorbent
surface is positively charged and the surface becomes anions
attracting/cation repelling. Conversely, above PZC the surface is
negatively charged and the surface becomes cation attracting/
anion repelling.
Zhu et al.130 explained that highest degree of decolourization
of methyl orange observed at pH 2 is attributed to the electrostatic attraction between the positively charged catalyst surface
and methyl orange anions, which led to the increase in degree
of adsorption and 97% photodecolourization. However, the dye
treatment results based on dye adsorption strength cannot be
explained as there are many other parameters operating at the
same time. For example, Muruganandham et al.133 found that
increasing pH from 1 to 9 increased decolourization rates for
reactive orange 4 (an anionic dye) from 25.27% to 90.49% aer
40 min and degradation from 15.16% to 87.24% within 80
minutes, respectively. However, the faster rate of color removal
and photodegradation was observed at alkaline pH. In contrast,
the degradation studies of some azo dyes showed conicting
results.134 For example, acid yellow 17 (an anionic dye) has
shown to be more degraded at pH 3, whereas, orange II (anionic
dye) and amido black 10B (anionic dye) showed maximum
degradation at pH 9.135
The pH can also affect whole photocatalytic dye degradation
mechanism and thus the degradation rate. For example positive
holes generated at lower pH act as major oxidation species,
however at higher or neutral pH range, hydroxyl radicals (OH_)
are largely responsible for oxidation process.136 On one hand,
these radicals can be generated in an alkaline solution,137
however, on the other hand sites the semiconductor surface
may not adsorb dye anions due to electrostatic repulsion
thereby decreasing their degradation and vice versa.138 It is
believed that hydroxyl radicals play an essential role in the
ssion of the –N]N– conjugated system in azo dyes in a TiO2
This journal is © The Royal Society of Chemistry 2014
View Article Online
Published on 05 August 2014. Downloaded by University of Birmingham on 26/08/2014 06:04:41.
Review
assisted photodegradation. The azo linkage (–N]N–) is mainly
vulnerable to electrophilic attack by hydroxyl radical. Riga
et al.109 reported that dye decolourization and degradation rate
increases with increasing pH. Whereas, at lower pH the
concentration of H+ exceeds and these H+ ions interact with azo
linkage reducing the azo group electron densities, resulting into
decrease in hydroxyl reactivity of hydroxyl radicals by electrophilic mechanism.
It has been reported that a dye with positive charge shows
higher adsorption rate on an unmodied TiO2 than for dyes
with a negative charge (anionic).139 It has been studied that
titanium dioxide has a higher oxidizing activity at lower pH;
however, excess of H+ at very low pH can decrease the rate of
reaction too. This can be explained by the characteristic of TiO2
particles that tend to agglomerate at lower or acidic condition,
which may reduce surface area of catalyst for maximum dye
adsorption as well as photon absorption.121,140,141 Bizani et al.142
reported that the pH effect on dye degradation rate can be
explained mainly by the modication of the electrical double
layer of the solid–electrolyte interface, which consequently
affects the sorption-desorption processes and the separation of
the photogenerated electron–hole pairs on the surface of the
semiconductor particles.142
Effect of pollutant adsorption strength
In heterogeneous photocatalysis, competitive adsorption
between water molecules and the target molecules that are to be
degraded plays an important role in photocatalysis.143,144 This is
due to the fact that photogenerated oxidizing species may not
migrate far away from their formation centres resulting into
negligible or a very slow rate of degradation at few nanometer
layers around the catalyst particles surface.145 However, in
various studies many authors have not reported a direct relationship between adsorption and photodegradation. In some
cases, adsorption of compounds or intermediates may acts as
poison on the catalyst surface. Vautier et al.146 reported that an
electrostatic interactions between the dye molecule and the
hydroxyl groups of the photocatalyst is always required for
proper dye adsorption.
Bizani et al.142 reported that strong adsorption may lead to a
multilayer of dye molecules around the catalyst particles
surface. This may result into limited interaction between
excited dye molecule and the catalyst in case of direct degradation mechanism or between incoming light and the catalyst
in case of indirect mechanism. In both of above cases the
photooxidation process is expected to decrease. This could be
the reason due to which the initial decolourization rate of the
dye is reported lower in acidic solutions. On the other hand, in
alkaline solutions, decrease in the initial rate of degradation
reects the difficulty of the anionic dye molecules to approach
the catalyst surface.147–149
RSC Advances
intensity, the rate of photocatalytic degradation increases.150–152
Collazzo et al.153 compared the direct black 38 dye degradation
ability of nitrogen doped TiO2 under visible light source and
sunlight. It was conrmed that nitrogen doped TiO2 due to its
higher absorption in visible region showed higher dye degradation (60% in 6 hours) under visible light. Under sunlight
irradiation, N-doped TiO2 exhibited degradation efficiency
slightly higher than non-doped TiO2 as shown in Fig. 4.
Effect of photocatalyst load
In order to avoid the excess use of the catalyst, it is necessary to
calculate optimum dose or loading of the catalyst for efficient
removal of dye. Off course the amount of catalysts required will
depend on the conguration of the reactor, light intensity, type
of the targeted dye and the type as well as particle morphology
of the catalyst. Owing to these many contributing factors there
are inconsistencies in the optimum catalyst dose used by
different researchers. Several authors have investigated the
function of catalyst loading on the reaction rate of photocatalytic oxidation process.133,154–156 Riga et al. reported that the
amount of dye adsorbed on catalyst surface generally increases
by increasing the TiO2 loading or the catalyst used. It was found
that generally TiO2 loading increases rate of photodecolourization, especially up to 1000 mg L 1 with an overall
60% TOC removal rate.109
Kaur et al.102 reported that in all of the optimized conditions
of efficiency, the catalyst dose for maximum photocatalytic
degradation of reactive red 198 is 0.3 g L 1. However, in another
study, the optimized condition for TiO2 consumption was
stated to be 0.5 g L 1.157 Mahvi et al.138 studied that an increase
in the amount of catalyst to the level constant with the optimized level of light absorption (normally 0.4 g L 1), increases
the amount of the decolourization.157–159 Also, Muruganandham
et al.133 reported that an increase of catalyst weight from 1.0 to
4.0 g L 1 increases the dye decolourization sharply from 69.27%
to 95.23% at 60 minutes and dye degradation from 74.54% to
97.29% at 150 min. A similar observation has been made by
other authors, as well.137,148,160
It is evident that initially photodegradation rate increases
with an increase in the amount of photocatalyst and then
decreases with increase in catalyst concentration (Fig. 5). This
trend can be explained by three possibilities:
Effect of light intensity
Band-gap sensitization mechanism does not have any inuence
on photocatalytic degradation rate or mechanism.101 However,
various studies have revealed that with an increasing light
This journal is © The Royal Society of Chemistry 2014
Fig. 4 Photocatalytic degradation of direct black 38 as a function of
time under visible light (left) and sunlight (right). Experimental conditions: Co ¼ 0.055 g L 1, Ccatalyst ¼ 1.0 g L 1, pH ¼ 2.5, T ¼ 25 C.153
RSC Adv., 2014, 4, 37003–37026 | 37009
View Article Online
RSC Advances
Review
Published on 05 August 2014. Downloaded by University of Birmingham on 26/08/2014 06:04:41.
Effect of inorganic salts
Fig. 5 Effect of increasing TiO2 catalyst loadings (in grams) on rate of
dye degradation.141
1 When all dye molecules are adsorbed on photocatalyst
surface, the addition of higher quantities of photocatalyst
would have no further enhancing effect on the degradation
efficiency.
2 Another possible reason could be due to the fact that an
excess of photocatalyst particles may increase opacity of the
suspension which may retard the degradation rate.161 Zhu
et al.130 reported in their study that as the amount of photocatalyst was increased from 0.05 to 0.5 g L 1 the number of
absorbed photons increased indicating 97% photocatalytic
decolorization of methyl orange solution. However, it was found
that at photocatalyst dosages above 0.5 g L 1, the rate constants
decreased due to the blocking of light penetration by the
excessive amount of photocatalysts.162
3 Moreover, particle–particle interaction becomes signicant
as the amount of particles in solution increases. This may result
in an enhanced rate of deactivation of activated molecules by
collision with ground state titanium dioxide particles and hence
decreases in dye concentration.141,163
Effect of the initial dye concentration
It has been reported earlier that by increasing the dye concentration, the decolourization rate constant (k) decreases.138 The
initial dye concentration can affect the rate of photodegradation
based upon two main aspects.
(1) In high dye concentrations, more active sites may be
covered with dye ions. This further may lead to the decrease in
the production of OH radicals on the surface of catalyst. Illinous
et al.164 studied the inuence of various initial dye concentrations for reactive yellow 125 dye on the photocatalytic discolouration and degradation in the concentration range of
0.025–0.1 g L 1. They concluded that increasing the dye
concentration will render the process less efficient by
decreasing degradation efficiency.
(2) Zhu et al.130 reported that the path length of the photons
entering the solution decreases as the initial concentration of
methyl orange increased. The reversal occurred for the lower
concentration, thereby increasing the number of photons
absorbed by the catalyst.132 The same {Zhu, 2005 #167} effect
was reported by Wang et al.165 during their study of the photocatalytic degradation of commercial dyes using zinc oxide
power as photocatalyst.
37010 | RSC Adv., 2014, 4, 37003–37026
The presence of mineral ions in dye contents of wastewater is
common. Some cations such as copper, phosphate and iron
have been reported to have the ability to decrease the photodegradation efficiency present in certain concentration. One of
the major reasons is that these substances may compete with
dyes for the active sites on the TiO2 surface and thus deactivate
the photocatalyst resulting in decreased degradation of targeted
dyes. Whereas calcium, magnesium and zinc have been studied
to have little effect on the photodegradation of organic
compounds which is associated to the fact that these cations are
present in their highest oxidation states causing no inhibitory
effect.166
The dye industry wastewater contains a considerable amount
of inorganic anions such as carbonates, chlorides, nitrate, and
sulphates. The presence of these salts causes colloidal instability, increases mass transfer and decrease in the surface
contact between the target dye molecule and the photocatalyst.166 Degradation of dyes decreases in the presence of
these ions. These CO32 and HCO3 ions may scavenge the HO_
radicals.24
CO32 + OH_ / CO3 _ + OH
(14)
HCO3 + OH_ / CO3 _ + H2O
(15)
CO3 _ + OH_ / HCO3
(16)
The decrease in degradation efficiency in the presence of
chloride ion is due to the hole scavenging properties of chloride
ion.
Cl + h+(VB) / Cl_
(17)
OH_ + Cl / HOCl_
(18)
HOCl_ + H+ / Cl_ + H2O
(19)
The chloride radical anions formed can also block the active
sites of the catalyst surface. The inhibitory effect of chloride and
phosphate ions on the photocatalytic degradation has also
already been reported.167 The inhibiting effect of CO32 ion is
greater than the inhibiting effect of Cl ion.
Wang et al.168 reported the effect of NO3 and SO42 on the
photodegradation of reactive red 2 dye under UV irradiation,
stating an increased in dye removal. Zhu et al.169 also reported
the same results that the presence of NO3 accelerated the
photocatalytic degradation of an azo dye under visible light
irradiation in their experiment. This can be attributed to the
direct or indirect hydroxyl radical formation as follow:
NO3 + hn / NO2 + O
(20)
NO3 + H2O + hn / NO2 + 2OH_
(21)
O + H2O / 2OH_
(22)
This journal is © The Royal Society of Chemistry 2014
View Article Online
Review
RSC Advances
Published on 05 August 2014. Downloaded by University of Birmingham on 26/08/2014 06:04:41.
SO42 in photocatalytic dye degradation has two important
roles. SO42 , by driving the dye molecule to bulk interface,
increases aqueous ionic strength that results into enhanced
photocatalytic efficiency. Also, the adsorbed SO42 reacts with
generated valence band holes forming SO4 . This reaction
between SO42 and photogenerated hVB+ on the photocatalyst
surface can prevent the electrons and holes recombination,
enhancing photodegradation rate as:
SO42 + h+(VB) / SO4 _
(23)
SO4 _ + H2O / SO24 + OH_ + H+
(24)
SO4 _ is a very strong oxidant with redox potential of +2.6 V,
which can enhance dye degradation. Further, the degradation
rates also depend on type of salt used. This effect has been
studied by various authors.109,133,138,170–172
Effect of addition of oxidizing species
Addition of powerful oxidizing species, such as hydrogen
peroxide (H2O2) and potassium peroxydisulfate (K2S2O8) to TiO2
suspensions is a well-known procedure which increases rate of
photooxidation.47,95,148,160,173 Hydrogen peroxide is believed to
have a dual role during the process of photocatalytic degradation. It accepts an electron from the conduction band, thus,
promotes the charge separation and it also forms OH_ radicals.
H2O2 + e / OH + OH_
(25)
H2O2 + O2 / OH + OH_ + O2
(26)
At H2O2 concentration greater than critical concentration, it
may act as hole or OH_ scavenger or react with TiO2 to form
peroxy compounds, which are detrimental to the photocatalytic
action.148,174–177 Bizani et al.142 reported that the addition of
oxidants such as H2O2 appears to be more effective in photocatalytic degradation of dyes than K2S2O8 comparatively,
although their effectiveness in decolourizing the solutions can
be reversed. Dye intermediates showed higher toxicity values
involving K2S2O8 than photocatalytic process involving H2O2,
indicating partial DOC (dissolved organic carbon) and toxicity
removal efficiency.
and their radial pulsation can be controlled by acoustic eld in
the resonating system.181 It has been observed that enhancement due to such synergistic mechanism is due to the deagglomerating effect of photocatalyst through ultrasound,
resulting into increased surface area and catalytic performance.182–185 However, industrial application of ultrasonically
induced cavitation is a problem due to ineffective distribution
of the cavitational activity on a large scale.186,187 Wang et al.168
studied the efficiency of combined treatment in which they used
photocatalysis and water jet cavitation on reactive red 2 dye
degradation. The results showed a signicant enhancement of
photocatalytic activity up to ca. 136%.
In hydrodynamic cavitation, cavitation is produced by pressure variations obtained by creating velocity variation and
decrease in static pressure that occurs when the uid passes
through a constriction.188 Saharan et al.189 reported that hydrodynamic cavitation is more energy efficient compared to
acoustic cavitation and has a higher degradation as for equivalent power/energy dissipation. In addition, other AOTs
including organic contaminants degradation using SO4 _ have
recently been introduced.190–193 These include radiolytic or
photolytic or thermal activation of persulfate or peroxide bond
to break it down to produce SO4 _. SO4 _ showed a higher
reduction potential of 2.5–3.1 V as compared with OH_ having a
standard reduction potential of 1.8–2.7 V. Moreover, it is more
selective for the oxidation of organic contaminants over a wide
range of pH.194,195 In addition, SO4 _ have a longer half-life,
depending on its preference for reactions related to electron
transfer, whereas OH_ with an equal preference participates in
every reaction.172,194,196
Development of efficient TiO2 photocatalysts by doping
There are various research studies on photocatalytic degradation of dyes using TiO2 in several modied forms for performance enhancement under visible light. These include
adsorption and surface complexation on TiO2, non-metal
doping, lanthanide ion doping, transition metal doping,
noble metal doping and multi-atom doping. The main purpose
of doping is to decrease the band gap of pure TiO2 (3.2 eV for
Strategies for enhancing photocatalytic
properties of TiO2
Photocatalysis by adopting advanced oxidation procedures
Recently cavitation methods have attracted attention as AOPs
for the removal of carcinogenic chemicals present in water.178,179
Cavitation involves the growth, nucleation and implosive
collapse of micro-bubbles and cavities that occur in fractions of
microseconds, releasing large amount of energy over a small
location that behave as micro-reactors.168 In acoustic cavitation,
pressure variations in liquid are effected through sound waves
(16 kHz to 100 MHz) using ultrasonic transducers as represented in Fig. 6. This produces oscillating bubbles of various
size moving at different velocities.180 The motion of the bubbles
This journal is © The Royal Society of Chemistry 2014
Fig. 6 Application of cavitation technology to photocatalysis by using
ultrasonic transducers for efficient treatment of organic contaminants.
RSC Adv., 2014, 4, 37003–37026 | 37011
View Article Online
RSC Advances
anatase phase) to bring the absorption band from UV to visible
region. The Fig. 7 below represents the simplied and relative
band position and band gap of pure, metal and non-metal
doped TiO2. The details about the doping methodologies and
photocatalysis mechanisms can be found elsewhere.197–199
Published on 05 August 2014. Downloaded by University of Birmingham on 26/08/2014 06:04:41.
Non-metal doping
There are various reports available on non-metal doping of
TiO2, especially with boron,200 carbon,201 sulfur, nitrogen and
uorine.202 The main objective of non-metal doping is to bring
the absorption band of TiO2 to visible region. Apart from its
advantages, however, long-term instability of the photocatalyst
is a major drawback.202 The detail about the dye degradation
including nitrogen and carbon doped TiO2 is given below under
separate headings.
Nitrogen doping. The nitrogen-doped TiO2 photocatalysts
have been tested for the decomposition of aqueous solutions of
organic compounds and dyes under UV and visible light illumination.201,203–207 Some examples of the N-doped TiO2 catalysts
used for different dye degradation studies along with their
preparation technique are given in Table 2.
Asahi et al. and others reported that nitrogen due to its
comparable size and electronegativity to that of oxygen is the
most suitable element for reducing the band gap width of
TiO2.216,217 Irie et al.218 proposed that an isolated narrow band
formed above the valence band in TiO2 xNx powder is responsible for the visible light response. In addition, increasing
nitrogen concentration lowered the quantum yield under UV
illumination, indicating that the doping sites could also work as
recombination centers. Parida and Naik219 reported the degradation of methylene blue and methyl orange using N-doped
TiO2 showing 67% and 59% of degradation aer 4 hours irradiation under visible light source. Selvaraj et al.220 measured the
photocatalytic degradation of the reactive triazine dyes
including reactive yellow 84, reactive red 120 and reactive blue
160 on N-doped TiO2 anatase and P25 in the presence of natural
sunlight. It was reported that reactive yellow 84 indicated a
faster degradation on N-doped TiO2 in sunlight thanthe
commercial Aeroxide P25. However, the P25 indicated higher
photocatalytic activity for the other two dyes. The COD level
within 3 h sunlight exposure, reduced to 65.1, 73.1, and 69.6%
for reactive yellow-84, reactive red 120 and reactive blue 160
respectively. In two separate studies, Ihara et al.221 and
Review
Serpone222 argued that synthesized nitrogen doped TiO2 with
the sites that were oxygen decient formed in the grain
boundaries were responsible for the visible light response,
whereas presence of nitrogen had only enhanced the stabilization of these oxygen vacancies. Songkhum and Tantirungrotechai223 prepared nitrogen and iron(III) co-doped TiO2 (N–
Fe–TiO2) and reported active for the photodegradation of
methyl orange. However, corresponding to the absorption
spectra the synthesized TiO2 photocatalysts except, under UV
irradiation, were not found to be photocatalytically active under
visible light irradiation. In summary, it can be concluded that,
apart from vague understanding of dye degradation mechanism
under visible light and various disadvantages, use of nitrogen
doped TiO2 may outweigh non-doped TiO2 in near future due to
its dye degradation activity under practically available
sunlight.224
Carbon doping. In recent years, dopants such as carbon and
nitrogen have received more attention owing to their low cost
with demonstration of narrow band gap which results in
signicant visible light absorption capability.225 Different routes
have been developed to synthesize carbon doped TiO2 which
can broadly be divided into two categories i.e. inner and outside
synthetic route. Inner approach includes incorporation of
carbon into TiO2 structure during its synthesis while outside
approach includes the incorporation aer TiO2 has already
been synthesised. Khan et al.226 manufactured carbon doped
TiO2 by controlled combustion of Ti metal in a natural gas
ame. Irie et al.218 prepared carbon doped anatase TiO2 nanoparticles by oxidative annealing of TiC under O2 ow at 873 K.
Sakthivel and Kwasch227 synthesized carbon-doped TiO2 nanoparticles by hydrolysis of TiCl4 with tetrabutylammonium
hydroxide followed by calcination of the precipitate obtained as
a result of wet process.
Ren et al.228 prepared doped TiO2 using outside preparation
approach. They added required amounts of amorphous TiO2,
glucose, deionized water in a Teon lined stainless steel autoclave by marinating the temperature at 160 C for 12 hours.
Velmurugan et al.229 recently synthesized carbon nanoparticle loaded TiO2 (CNP–TiO2) through sonochemical
method. CNP–TiO2 was found to be stable and reusable.
Comparatively, photocatalytic activity of CNP–TiO2 under solar
light for degradation of reactive red 120 was found higher than
TiO2 P-25 and as prepared TiO2. Increase in activity was related
to suppression in recombination of photogenerated electron–
hole pair by loaded CNP indicated by a decrease of measured
photoluminescence intensity.
Lanthanide ions doping
Fig. 7 Simplified relative energy bad positions and band widths for
pure (hn) metal doped (hnm) and non-metal doped (hnnm) TiO2
anatase.197
37012 | RSC Adv., 2014, 4, 37003–37026
Lanthanide ions are known for their complex formation with
various Lewis bases e.g. aldehydes, acids, amines, alcohols,
thiols. These Lewis bases interact with the f-orbitals of the
lanthanides through their functional groups. Thus, incorporation of lanthanide ions into a TiO2 matrix could provide a mean
to concentrate the organic pollutant at the semiconductor
surface and consequently enhance the photoactivity of
TiO2.230–232 It has been reported in literature that the optimum
This journal is © The Royal Society of Chemistry 2014
View Article Online
Review
Published on 05 August 2014. Downloaded by University of Birmingham on 26/08/2014 06:04:41.
Table 2
RSC Advances
Studies on N-doped TiO2 assisted photodegradation of different dyes
Catalyst
Dyes used for analysis
Techniques for preparation of N-doped TiO2 catalysts
Ref.
N-Doped TiO2
N-Doped anatase and rutile
N-Doped TiO2 nanotubes
Microarrays of N-doped ower-like TiO2
N-TiO2
N-TiO2 nano colloid
N-TiO2
N-TiO2
N-TiO2
Rhodamine B
Methyl blue
Methyl orange
Methyl orange
Methyl orange and phenol
Methyl blue
Ethyl blue and 4-chlorophenol
Methyl blue
Rhodamine B
Microemulsion-hydrothermal method
Calcination of acidied TiCl3 in presence of urea and oxalic acid
Solvothermal process
Electrochemical anodization of Ti in NH4F aqueous solution
Microwave method
Nitridation of a porous TiO2
Sol gel using NH4Cl as nitrogen source
Simple method
Plasma based ion implantation
208
209
210
211
212
213
207
214
215
level of rare earth metal doping is 1–2% to hinder the crystal
growth of TiO2 during calcinations.202 Although doping of
lanthanide ions into TiO2 attracted some attentions still such
works are little so far. Additionally, lanthanides ions can in fact
trap conductive band electrons when restricted to the TiO2
surface.233 Recently, La3+, Nd3+, Sm3+, Eu3+, Gd3+, and Yb3+
modied TiO2 nanoparticles with their ability to increase the
anatase phase stability and preventing the segregation of TiO2
have excessively been investigated for maximizing the efficiency
of photocatalytic reactions.234–236 Xie et al.237,238 prepared three
types of lanthanide ion-modied titanium dioxide i.e. Eu3+–
TiO2, Nd3+–TiO2 and Ce4+–TiO2 and tested for the photodegradation of azo dye X–3B under visible light irradiation. The
results showed that Lnn+–TiO2 system had a higher photocurrent generation. They ranked reaction rates as Nd3+–TiO2 sol >
Eu3+–TiO2 sol > Ce4+–TiO2 sol > TiO2 sol > P-25 TiO2 powder.
Zhang et al.239 prepared TiO2 particles co-doped with boron and
lanthanum (B–La–TiO2) at a molar ratio of 1 : 4 and investigated
their photocatalytic performance to photodegrade methyl
orange dye. The result showed organic dye degradation to 98%
within 90 min compared to 24% with undoped TiO2. It was
speculated that the reason behind enhanced photocatalytic
activity of B–La–TiO2 photocatalyts is its excellent photocatalytic
effect under the visible light region.
Very recently, Lan et al.240 successfully prepared lanthanum
and boron co-doped TiO2 (La–B–TiO2) by modied sol–gel
method to enhance the visible-light photocatalytic performance
by improving the quantum efficiency of the photocatalytic
reaction. 1% La–B–TiO2 catalysts showed highest photocatalytic
degradation of acid orange 7 up to 93% under visible-light
irradiation for 5 h. Nasir et al.241 synthesized 0.1 Ce/C codoped TiO2 via hydrothermal method for the efficient degradation
of an aqueous solution of acid orange 7 dye under visible light
irradiation. Co-doped catalysts showed higher photocatalytic
activity compared to C-doped catalyst. However, increasing Ce
concentration above 0.1 Ce/C–TiO2 resulted in an increase of
electrons and holes recombination. In another study Nasir
et al.242 again used Ce to prepared Ce–S co-doped TiO2 because
of its Ce3+/Ce4+ redox couple, which contains the ability to shi
between Ce2O3 and CeO2 under reducing and oxidizing conditions.243 Results indicated that decrease in the particle size,
increase in the surface area, abundance of surface hydroxyl
This journal is © The Royal Society of Chemistry 2014
groups, and reduction of recombination of e and h+ assisted
the enhanced photocatalytic degradation of acid orange dye.
Transition metal doping
Incorporating transition metals in the TiO2 crystal lattice may
result in the formation of new energy levels between valence
and conduction band, inducing a shi of light absorption
towards the visible light region. However, it has been reported
as well that transition metals may cause thermal instability for
the anatase phase of TiO2.244
Cadmium doping. Cadmium is one of the heavy metals
which could be present in real dyes containing wastewater. It
can modify the photocatalytic activity of the catalyst by being
absorbed on the photocatalyst surface.245 Andronic et al.245
investigated the photocatalytic efficiency of cadmium doped
TiO2 thin lms obtained using the doctor blade deposition
method to degrade methyl orange and methylene blue dyes.
Results showed a linear correlation between the band gap
energy of the cadmium doped TiO2 lms and dyes photodegradation efficiency. Some authors have reported negative or
overall no effect of cadmium ion on the photocatalytic
activity.246 However, these effects highly depend on the
cadmium concentration and doping method used. More studies
are needed to understand the system completely as Cd may be
oxidized to CdO which is a p-type semiconductor thus modifying the electronic properties of the system.
Copper doping. It has been reported that Cu(II) has the
ability to extend the light absorption to visible region by
modifying the TiO2 valence band spectrum resulting into
improved photocatalytic activity.247–249 Copper sulphides have
also largely been investigated in recent years due to their
remarkable optical and electrical properties as a result of variations in composition, morphology, stoichiometry and their
potential applications as absorbers for solid state solar
cells.250,251 Andronic et al.252 studied the photocatalytic process
by using CuxS and coupled CuxS/TiO2 thin lms for methyl
orange and methylene blue photodegradation. The photocatalytic activity of CuxS/TiO2 nanocomposites depended on
CuxS : TiO2 ratio. The best results were achieved under UV
irradiation, when H2O2 is added in photocatalytic process at
CuxS : TiO2 ¼ 3 : 7, with high degradation efficiency of almost
99% using methyl orange in 300 min and methylene blue in 180
RSC Adv., 2014, 4, 37003–37026 | 37013
View Article Online
Published on 05 August 2014. Downloaded by University of Birmingham on 26/08/2014 06:04:41.
RSC Advances
min. This semiconductors association and the lms homogeneity have the ability to limit the electron–hole recombination
facilitating good efficiency in dyes photodegradation even
under visible light irradiation. Huang et al.253 prepared Cu2O
nanoparticles and microparpicles. They tested these particles
for the photodegradation of methyl orange. It was observed that
nanoparticles were stable in ambient atmosphere, whereas
microparticles were found stable as a Cu2O/CuO core structure.
The Cu2O microparticles with very slow photocorrosion rate
exhibited a higher photocatalytic activity for methyl orange dye
than that of the deactivated nanoparticles during the photocatalytic reaction.
Sn4+ doping. Sn4+ doped nanosized TiO2 particles have
several advantages compared to other TiO2 powders. They have
pure anatase crystalline form having high-dispersion ability
both in polar or non-polar solvents. They also have ne particle
size with more uniform distribution with stronger interfacial
adsorption facilitating its easy coating on different supporting
material.254 The Sn4+-doped TiO2 nanoparticles having molar
doping ratio for Sn4+ and tetrabutylorthotitanate of ca. 5 were
synthesized by hydrothermal process at 225 C. The double
layers of these nanoparticles coated on glass surfaces were
found to be having much higher photocatalytic performance
under UV and Vis lights than pure TiO2.
Noble metal modied TiO2
Deposition of noble metals on TiO2 surface has been reported to
improve the photocatalytic efficiency by acting as an electron
trap due to the Schottky barrier formation thereby reducing
electron–hole recombination process and helping interfacial
charge transfer.79,255–261 TiO2 modied with noble metal exhibits
excellent stability as well as high reproducibility. Doping of TiO2
with noble metals for photo-oxidation has been studied for at
least two decades. However, the detail about the most recent dye
degradation work including Silver and Platinum doped TiO2 is
given below under separate headings.
Silver modied TiO2. Silver modied TiO2 has shown
promising results towards increased degradation efficiency and
stability. Gupta et al.262 were able to regenerate Ag+ doped TiO2
catalyst just by washing the catalyst thoroughly with distilled
water. Photocatalytic activity of Ag+ doped TiO2 indicated >99%
decolorization of basic violet 3 and methyl red within 90 min
with a 86% mineralization efficiency. Seery et al.255 reported an
enhanced decolorization of rhodamine 6 G with Ag modied
TiO2 under visible light photocatalysis. Increase in decolorization is attributed to the increase in visible absorption capacity
of silver nanoparticles. Whereas, Gunawan et al.263 demonstrated the reversible photo-switching of nano silver on TiO2.
Reduced silver on a TiO2 support when exposed to visible light
(l > 450 nm) resulted in electron excitation and its reverse ow
to the TiO2 support from silver by oxidizing silver (Ag0 / Ag+) in
the process. For improved optical properties it would be more
attractive to further tailor the band gap width of TiON/Ag2O
with some potential transition metals.264
Platinized TiO2 nanoparticles. Platinum deposited TiO2 has
been repeatedly used in a variety of photoreactions that speeds
37014 | RSC Adv., 2014, 4, 37003–37026
Review
up the water splitting reaction265,266 and oxidation of organic
compounds145,267,268 and CO.269 Platinum nanoparticles can be
benecial for the subsequent oxidative reaction steps in the
presence of molecular oxygen, which allows direct oxidation of
the organic compounds by holes and HO_ radicals as well. The
main effect of Pt-loaded TiO2 is due to its higher production rate
of oxidizing species, e.g. holes or HO_radicals than conventional
heating operation.
Multi-atom doped TiO2
Many studies have revealed that TiO2 mono-doping may lead to
recombination centers thereby inhibiting light-induced migration of charge carriers to the surface.270 However, it has been
recognized that co-doping of TiO2 with both nonmetal and
metal can reduce the number of recombination centers by
neutralizing positive and negative charges inside the TiO2,
which can effectively improve the efficiency of migration of the
charge carriers and thus enhance photocatalytic activity.271 Xing
et al.272 prepared carbon and lanthanum co-doped TiO2 by a
hydrothermal method and reported their high photocatalytic
activity under both UV and visible-light irradiation. Recently,
Yang et al.273 synthesized Mo and C co-doped TiO2 photocatalysts and reported that 1% Mo–C4/TiO2 showed an excellent
visible light photocatalytic degradation of rhodamine B dye.
The prepared co-doped catalysts showed greater photocatalytic
activity than pure anatase TiO2 and the mono-doped catalysts,
because a synergistic effect between molybdenum and carbon
increases absorption of visible light and affects separation of
photoinduced electrons and holes. Also, Yan et al.274 investigated photocatalytic degradation of methyl orange by TiO2–
SiO2–NiFe2O4 suspensions and reported that OH_ radicals and
h+ plays important roles in the degradation by TiO2–SiO2–
NiFe2O4. Akpan and Hameed275 compared electronically stable
composite photocatalyst of the type Ti(1 x y)Ca(3x y)Ce(2x y)–
W(y/6)O2(1 2(y x)) (at y < 2x and x + y < 1) prepared by sol–gel
method with commercially available Degussa P-25 and TiO2
photocatalysts for acid red 1 (AR1) photocatalytic degradation.
The performance of the composite catalyst excelled that of TiO2,
but was as good as Degussa P-25 in terms of the solar photodegradation. However, composite photocatalyst was found
better than Degussa P-25 in terms of reusability since it could
settle out of solution in less than one hour aer solar experiment. The composite photocatalyst was found to have narrowed
band gap as compared to TiO2 by 0.26 eV with its activities more
into visible region.
Dye sensitization in photocatalysis
On a broader scale, waste water remediation with dye sensitization method is benecial in two ways. Firstly, the adsorption
of the dye on the surface of TiO2 catalyst extends the absorption
spectrum of TiO2 from UV to visible regime.102 Secondly, the
system containing the dye and the phenolic compound represents a classic model of a real effluent stream, which is usually a
mixture of different organic compounds, surfactants and metal
ions. Dye sensitized degradation is primarily aided by enhanced
adherence of the dye molecule onto TiO2 surface in the presence
This journal is © The Royal Society of Chemistry 2014
View Article Online
Published on 05 August 2014. Downloaded by University of Birmingham on 26/08/2014 06:04:41.
Review
of O2 that can easily scavenge the injected electrons from the
conduction band of TiO2.76 General mechanism of dye sensitized photocatalysis has been explained in detail in basic principles and mechanism section of this review. Zhang et al.276
recently studied the aerobic selective oxidation of alcohols in
the presence of an anthraquinonic dye (alizarin red S) sensitized
TiO2, and a nitroxyl radical (2,2,6,6-tetramethyl-piperidinyloxyl).
They found that the whole mechanism involved was the
formation of a dye radical cation, which oxidized the nitroxyl
radical. This oxidized radical species was found to be mainly
responsible for the selective oxidation of alcohols into aldehydes. Other conjugated polymers such as poly(aniline)277 and
poly(thiophene)278 has also been used as TiO2 sensitizers for the
degradation of dyes.
Recently, there have been new discoveries related to the
adsorption of complexants on TiO2 surface leading to a sharp
enhancement in its activity under visible light by using absorbent
such as salicylic acid.279 In a study, Moser et al.280 proved that
surface complexation of colloidal semiconductors strongly
enhance interfacial electron transfer rates. Ikeda et al.281
demonstrated that phenolic compounds with TiO2 can work as
catalyst under visible light below ca. 550–600 nm for water
reduction in the presence of a sacricial donor. Also, Zhang
et al.282 chemically modied TiO2 nanoparticles with catechol (4.0
wt% catechol/TiO2) without changing the crystalline structure of
TiO2. Surface complexation of catechol lead to an enhanced
acid orange 7 dye photocatalytic degradation by shiing onset
wavelength of the optical absorption to the visible range.
Structurally modied TiO2
For enhancement of photocatalysis, nanostructured materials
with different shapes of TiO2 including nanoparticles, nanotubes, nanobers, nanocages, nanorods, nanorings, nanosheets, nanocombs, nanobowls, nanosprings and nanobelts
have been employed.283 The discussion below illustrates the use
of most common TiO2 structural modication to enhance its
photocatalytic activity. TiO2 can be synthesized in the form a
nanometer scale tube like structure called TiO2 nanotubes.284
The photoactivity of the TiO2 nanotube lms has been found as
strongly inuenced by the tube diameter and thickness.285,286
Increasing tube thickness increases the photodegradation efficiency till a maximum and then decreases till a steady value. In
much longer tubes active species have a longer diffusion path
that may cause the decrease in photocatalytic degradation rate.
The nanotube arrays have been found to be more active than
anatase or P-25 TiO2 nanoparticulate lms with similar thickness and geometric area. The enhanced dye degradation activity
is attributed to a more effective separation of electron–hole
pairs taking place in a well ordered way in TiO2 nanotube array
lm and due to higher internal surface area of the nanotube
structure.285–290
Graphene modied TiO2
Carbon can also be used in the form of graphene to synthesize
graphene/TiO2 photocatalysts.291 Graphene is an atomic sheet of
sp2-bonded carbon atoms with unique properties having high
This journal is © The Royal Society of Chemistry 2014
RSC Advances
conductivity, large specic surface area and high transparency
due to its one-atom thickness.292 Zhang et al.293 prepared a P-25–
graphene composite by hydrothermal treatment of a suspension of P-25 and graphene oxide. Graphene oxide was reduced
to graphene and then P-25 nanoparticles were deposited
simultaneously on this graphene sheet. The P-25–graphene
composite was found more active than P-25 for the photodegradation of methylene blue due to reduced charge recombination and enhanced absorptivity. The P-25–graphene
composite exhibited higher efficiency than P-25 having same
carbon content, due to its giant two-dimensional planar structure, which facilitated a better platform for the adsorption of
the dye and charge transportation.283 Moreover, TiO2/graphene
composites have been well studied as a solar light photocatalysts and electrode materials for lithium-ion batteries.
Recent reports have shown that ultralight 3D-graphene aerogels
(GAs) can better adsorb organic pollutants and can provide
multidimensional electron transport pathways. Qiu et al.294
prepared 3D-structured TiO2/GA composites by one-step
hydrothermal method using glucose. Glucose acts as facetcontrolling agent to achieve in situ growth of TiO2 nanocrystals on GAs surfaces. TiO2 nanocrystals exposed with {001}
facets and mesoporous structure were highly dispersed on the
GAs surface. Affording high surface area, massive appearance,
and hydrophobic properties determine its high recyclability and
to efficiently photodegrade methyl orange dye.
Fullerenes modied TiO2
A fullerene is anymolecule composed entirely of carbon, in the
form of a hollow sphere, ellipsoid, tube, and many other shapes.
Spherical fullerenes are also called buckyballs. Cylindrical
fullerenes are calledcarbon nanotubes or buckytubes. Fullerenes are similar instructure to graphite, which is composed of
stackedgraphene sheets of linked hexagonal rings; but they may
also contain pentagonal or sometimes heptagonal rings.
Fullerenes are extremely hydrophobic, therefore, their use in
aqueous media is quite limited. However functionalizing the
molecules with hydroxyl groups can improve water solubilizing
properties of fullerenes.283 Krishna et al.295 employed polyhydroxy fullerenes (PHF) to enhance the photocatalytic efficiency of TiO2 for the degradation of the procion red dye. The
PHF molecules adsorbed on the surface of TiO2 by electrostatic
forces enabled the scavenging of the photogenerated electrons
decreasing the electron/hole recombination. The surface
coverage of the TiO2 nanoparticles by the PHF molecules
(C60(OH)n, n ¼ 18–24) determined the extent of enhancement in
dye degradation, with an optimum PHF/TiO2 weight ratio equal
to 0.001.296,297
Improvement by enhancing TiO2 reactive facets
For anatase TiO2, theoretical and experimental studies have so
far revealed that {001} facet compared to thermodynamically
stable {101} facet is much more reactive being the dominant
source of active sites for various applications.298 Whereas, most
of the synthetic anatase crystals due to its crystal growing
process are dominated by the less-reactive {101} facets
RSC Adv., 2014, 4, 37003–37026 | 37015
View Article Online
Published on 05 August 2014. Downloaded by University of Birmingham on 26/08/2014 06:04:41.
RSC Advances
diminishing the reactive {001} facets to minimize the surface
energy. Chen et al.299 presented a simple hydrothermal
approach for synthesizing uniform, hierarchical spheres selforganized from ultrathin anatase TiO2 nanosheets with nearly
100% exposed {001} facets. Also, Liu et al.300 reported fabricating hollow TiO2 microspheres composed of anatase polyhedra with 20% exposed {001} facets by uoride-mediated selftransformation method, exhibiting tunable photocatalytic
selectivity in decomposing azo dyes in water. Very recently, Yu
et al.301 synthesized of layered TiO2, composed of nanosheets
with exposed {001} facets, by a simple hydrothermal method. It
was observed that layered TiO2 with {001} facet nanosheets
exhibited excellent photocatalytic activity for the degradation of
rhodamine B dye.
Practical aspects of TiO2 photoprocesses
Limitations of TiO2 photo-processes
Performance of a catalyst depends upon its congurations i.e.
suspended or xed-bed catalyst impart different performances.
Although, coating a catalyst eliminates the need for its postltration and centrifugation but it generally reduces the
system efficiency signicantly largely due to loss in exposed
surface area.302,303 On the other hand disadvantages using
powder form of catalyst include stirring during the reaction and
separation of catalyst from the treated water aer each run. To
address the later, ltration, sedimentation and centrifugation
processes have been used to recover highly dispersed and suspended catalyst from the treated water. However, with this
method a fraction of TiO2 particles usually remains in the
treated water and a further microltration step is usually
required for nal purication. Besides its time consuming
problem, the ltration process become increasingly inefficient
as the particle size diminishes. Smaller particles suspended in
the water may penetrate through ltration materials causing
membranes lter clogging.304
The other common way to perform the separation is by
sedimentation of TiO2 particles aer pH adjustment by coagulation–occulation process. Separation by sedimentation has
been enhanced by attaching TiO2 particles onto other support
particles like quartz, silica gel, alumina, zeolites, activated
carbon or glass spheres but the loss of photocatalytic activity
has usually been observed.305 In addition to this the fast
aggregation of TiO2 in suspension leads to a decrease in effective surface area which reduces its catalytic efficiency. A ltration step aer photocatalytic reaction is still required because of
TiO2 suspension.164 Moreover, TiO2 absorption wavelength
corresponding to the band-gap energy of 3.02 eV is at near
ultraviolet radiation.306 Thus either the need of an UV excitation
source or ability of TiO2 to absorb only 5% energy of the solar
spectrum has restricted its technological applications.
Trends in improving TiO2 photo-processes
Despite of drawbacks discussed in the above section, more
coated photocatalysts and immobilization techniques are still
37016 | RSC Adv., 2014, 4, 37003–37026
Review
been investigated.164,307–311 In many cases TiO2 coated on a
support is found to be more efficient for organic compound
removal in contrast to uncoated TiO2, reducing overall operating costs.312 Many researchers have examined some methods
for xing TiO2 on supporting materials including glass beads,313
ber glass,161,314 activated carbon,315 silica316 and zeolite317 as
given in Table 3.
Zeolite as TiO2 support
Zeolites are thealuminosilicate members of the family of
microporous solids known as molecular sieves. The termmolecular sieve refers to the ability to selectively sort molecules
based primarily on a size exclusion process. This is due to a very
regular pore structure of molecular dimensions. Among variety
of supports available, zeolites are considered to provide an
effective electric eld of their framework for separation of
photogenerated electrons and holes.318,324 However care should
be taken while using zeolite as TiO2 support so that it may not
affect the TiO2 photoactivity and the adsorptive properties of
zeolite. Mathews325 reported that photoefficiency of TiO2 is
suppressed when Ti interacts with zeolite. The OH_ available on
the surface of TiO2 can be easily transferred onto zeolite surface
as shown in Fig. 8. Additionally, the presence of zeolite on TiO2
maintains dye molecules near the photocatalyst (local concentration effect) which may result in an increase of degradation
rate.
TiO2 loaded hydrophobic mesocellualr foams
Hydrophobic materials based on zeolites and mesoporous
silicas such as hexagonal mesoporous silica (HMS), SBA-15 and
mesocelluar foams could offer excellent ability of adsorption of
organic compounds owing to their weak adsorption of water
molecules and the large surface areas.326 Though simple surface
uorination on TiO2 can induce an enhanced UV light photocatalytic oxidation activity, however it is difficult to improve the
visible light photocatalytic activity of TiO2, owing to the lack of
photo-excited holes in the visible light irradiation.327
In 2012, Xing et al.328 prepared a novel hydrophobic TiO2
photocatalyst, which can enhance visible light response by
using cheaper and low-toxic inorganic NH4F. They prepare the
super-hydrophobic mesocellular foams loaded with nanosized
TiO2 photocatalyst. Mesoporous catalyst greatly facilitated the
surface uorination, which together with Ti3+ (a self-doped TiO2
catalyst) generation promoted its visible light photocatalytic
activity329 and the surface uorination enhanced UV light photocatalytic activity. It was reported that the catalyst exhibit
permanent and excellent super-hydrophobic property, high
adsorption capacity, and enhanced photocatalytic activity for
rhodamine B (RhB) degradation. Recently, Qi et al.330 prepared
carbon-doped TiO2/mesocellular-F photocatalysts hydrophobically modied by the hydrothermal method. Catalyst indicated
an efficient visible light photodegradation of methyl orange
solution because of the synergistic effect of small crystal size,
carbon dopants, and hydrophobic modication due to the
uorination of NH4F.
This journal is © The Royal Society of Chemistry 2014
View Article Online
Review
Published on 05 August 2014. Downloaded by University of Birmingham on 26/08/2014 06:04:41.
Table 3
RSC Advances
Types of the supports used for enhancing TiO2 photocatalytic degradation of different dyes
Support type
Dye used for degradation
Technique used for
preparation
Clinoptilolite (CP) (Iranian
Natural Zeolite)
Acid red 114
—
Chitosan [b-(1/4)-2-amino2-deoxy-D-glucose]
Methyl orange
Solution casting technology
Polymethylmethacrylate
(PMMA) rings
Methylene blue
Ultrasonically spray-coated
with TiO2 sol
Polyamide 6 (PA6) ber
Methylene blue
Low temperature
hydrothermal method
Glass plates
Acid red 27 (AR27)
Immobilized
Non-woven paper with SiO2
Reactive black 5 (RB5)
—
Sand
Methylene blue, rhodamine
B and methyl orange
—
Performance
Ref.
TiO2/clinoptilolite (SSD)
proved to be an active
photocatalyst with a rst
order reaction, k ¼ 0.0108
min 1. With increasing dye
conc. photodegradation
conversion of AR 114
decreased
The TiO2/ZnO/chitosan
NTFs showed high
photocatalytic activity under
solar irradiation
Results showed 80%
degradation of methylene
blue aer 10 min at pH 9
Compared with the
untreated fabric, the
protection against UV
radiation improved. The
titanium dioxide coated
fabric could degrade
methylene blue efficiently
dye under UV irradiation
Outlet stream from
photoreactor was
mineralized with products
such as NH4+, NO3 , O2 and
SO42 ions
Degradation of RB5 azo dye
was strongly inuenced by
the ionic strength of the
solution. Above pH PZC of
SiO2, the cations of the
solution increased the
amount of dye adsorbed
onto the photocatalyst
support
TiO2/UV process supported
on sand is effective in totally
mineralizing these
compounds
318
319
320
321
322
170
323
Chitosan as TiO2 support
Chitosan [b-(1/4)-2-amino-2-deoxy-D-glucose] is a natural
cationic biopolymer that is produced by N-deacetylation of
chitin. Chitin is considered as the second most abundant
natural polysaccharide aer cellulose.331 The extraction of chitin
from shells and its subsequent deacetylation to chitosan is a
relatively low cost process.332
Fig. 8 Synergistic effect of TiO2 and clinopitilolite catalyst on dye
degradation by producing OH_ free radicals.318
This journal is © The Royal Society of Chemistry 2014
Chitosan molecules contain a large number of reactive
hydroxyl (–OH) and amino (–NH2) groups. Also, chitosan has
RSC Adv., 2014, 4, 37003–37026 | 37017
View Article Online
Published on 05 August 2014. Downloaded by University of Birmingham on 26/08/2014 06:04:41.
RSC Advances
high affinity for metal ions and this property has been used to
prepare metal–chitosan nanocomposites.333 This enables Chitosan to exhibit unique adsorption and chelating properties for
all kinds of heavy metal ions,334–336 making chitosan an appropriate and excellent bio-matrix for synthesizing nanosized
particles for various inorganic photocatalysts such as titanium
oxide,337,338 cadmium sulde,319,339 zinc sulde,340 zinc oxide341
and cuprous oxide.342 In addition, immobilizing nanosized
photocatalysts onto chitosan bio-matrix can effectively prevent
agglomeration of nanoparticles during growth and can overcome the difficulties related to separation and recovery of
nanosized powder materials.336
Activated carbon as TiO2 support
Activated carbon also known as activated charcoal (AC) is a
highly porous form of carbon with porosity spanning the macro
(l > 50 nm), meso (0.5–1 mm) and micro (<1 mm) pore ranges116
and very high-surface typically up to 900–1200 m2 g 1.343 It is
generally produced from cheap carbonaceous source materials
such as nutshells, coconut husk, peat, wood, coir, lignite, coal,
and petroleum pitch. Use of activated carbon is the most
common method applied for dye removal by adsorption.344 In
particular, activated carbon (AC) has been extensively
researched as a support for heterogeneous catalysis,345 and
there exists over 650 studies and well over 1000 patents346 concerning AC–TiO2 mixtures or composites.347–351 Due to its higher
effectiveness, it has been applied on adsorbing cationic,
mordant, and acid dyes and to dispersed, vat, direct, pigment
and reactive dyes on a slightly lesser extent.26,352
Effective performance using activated carbon mainly
dependents upon the type of carbon being used and the
characteristics of the aqueous solution containing various
chemicals and non-targeted contaminants. Regeneration or
reuse can result in a steep reduction in performance, and
efficiency of dye removal. Activated carbon, like many other
dye-removal treatments is considered suitable for one particular type of pollutant or waste system and ineffective on
another. Although, activated carbon is expensive it comes with
the advantage of regeneration. However, this reactivation
usually results into 10–15% loss of the sorbent. Arana et al.353
prepared AC and TiO2 catalysts having varying proportion. The
results showed that the AC in addition to increasing surface
area can also modify the acid–base properties and the UV
spectrum of TiO2. It was reported that activity of AC was
increased under solar irradiation.
In AC–TiO2 system, the adsorption capacity of AC enhances
the chances of high concentration of reactants to come in
contact with TiO2 and possibly turning them into their intermediates as explained in the Fig. 9. Zhang et al.236 proposed a
similar illustration for the photocatalyzed mineralization of
methyl orange to understand the effect of presence of AC onto
TiO2 for effective dye degradation. On the other hand, a disadvantage of using AC is the excessive formation of nanosized
pores resulting into rare inltration, leaving TiO2 on the outer
macropores.116,354,355 Moreover, the band gap tuning problem of
TiO2 is not resolved by the use of AC as a support.
37018 | RSC Adv., 2014, 4, 37003–37026
Review
Fig. 9 Synergistic mechanism between AC–TiO2 composites. The
arrow labelling un-reacted emphasizes that in the absence of Absorbent the reactants may remain un-reacted into the solution resulting in
low photoactivity of methyl orange.236
Silica as TiO2 support
Use of supported TiO2 catalysts depends on the nature of
supports, one of the most important factors inuencing photocatalytic performance.169,356,357 Recently, amorphous SiO2 due
to its special physicochemical properties such as high adsorption capacity has been studied showing advantages towards
highly active support for catalysts. The presence of considerably
large number of acid sites and hydroxyl groups on the surface of
amorphous SiO2 material make it more absorptive.358,359 Studies
have shown that silica gel can be an effective support for
binding TiO2 that is effective for removal of basic dyes.
However, in such processes, there can be side reaction taking
place along with photocatalysis and therefore such limiting
factors can prevent its commercial application.26 Additionally,
immobilization TiO2 on a suitable and inert matrix has shown
an advanced organic and inorganic pollutant photodecomposition than that of pure TiO2.169,360
Sun et al.361 investigated the catalytic properties of three
porous amorphous silica including diatomite, opal and porous
supported photocatalysts (TiO2/SiO2) by UV-assisted degradation of rhodamine B. Through morphology and physical properties of the resulting TiO2/amorphous SiO2 catalysts, it was
suggested that the nature of silica supports could affect the
particle size and the crystal form of TiO2. TiO2/diatomite photocatalyst, compared with pure TiO2 (P-25) and the other two
TiO2/amorphous SiO2 catalysts, exhibited better catalytic
performance at different calcination temperatures with a discolouration rate of up to over 85%. Photocatalytic properties
such as mixed-phase TiO2 with small particle size might be
responsible for efficient performance. Furthermore, its stable
and inert porous structure improves its activity.
Carbon nanotubes as TiO2 support
The carbon nanotubes (CNTs) are interesting materials having
unique electronic properties associated with their special 1D
structure which facilitates the charge transfer.362 The CNTs are
described as tubular assemblies made exclusively of rolled-up
lms of interlocked carbon atoms. These are classied as
single-walled carbon nanotubes (SWCNTs) which consist of a
This journal is © The Royal Society of Chemistry 2014
View Article Online
Published on 05 August 2014. Downloaded by University of Birmingham on 26/08/2014 06:04:41.
Review
single layer of graphene sheet rolled into a cylindrical tube or
multi-walled carbon nanotubes (MWCNTs), which contain
multiple concentric tubes. CNTs have a large specic surface
area due to their hollow geometry. CNTs–TiO2 hybrids have
been tested for the photodegradation of acetone,363 methylene
blue364,365 and phenol.366,367 All such studies emphasized that the
addition of CNTs had enhanced the photocatalytic effectiveness
of TiO2.
Yu et al.368 compared the effect of MWCNTs on the adsorption and the photocatalytic properties of TiO2 P-25. The results
showed that the mixture of CNTs and TiO2 signicantly
improved the photocatalytic activity of TiO2 for the treatment of
three azo dyes and was found more efficient than the mixture of
TiO2 with activated carbon. Luo et al.369 prepared short
MWCNTs that can be suspended, sorted and manipulated more
easily so that the light can well penetrate into the inner tubes.
The short MWCNTs were used as initial materials to fabricate
TiO2/short MWCNTs nano-composites that were tested for the
photodegradation of reactive brilliant red X-3B. The photoactivity of the TiO2/short MWCNTs samples with optimum
weight ratio (1 : 100) was studied and rates much higher than
that of various active photocatalysts (TiO2/short MWCNTs >
TiO2/MWCNTs > TiO2> P-25) were reported.
TiO2 embedded in polymer matrix
Difficulties such as low quantum yield and low adsorption
capacity of TiO2 photocatalyst limits its practical application.122
Among multiple techniques to overcome these issues, incorporation of semiconductors into the polymer matrix have been
achieved. Example such as polypyrrole (PPy)–TiO2 composite
lms, polyethylene–TiO2, and polyvinylchloride (PVC)–TiO2 as
resulting composites were found to enhance degradation reactions more effectively than a suspension of TiO2 nanoparticles.370 Cheng et al.371 report efficient adsorption and
photodegradation of textile dyes orange II and methyl orange
under UV irradiation using polyaniline (PANI) and PANI–TiO2
composite nanotubes as photocatalyst, respectively. Decolorization up to 98.6% of orange II and 98.1% of methyl orange in
the presence of PANI–TiO2 composite nanotubes were reported.
Addition of TiO2 nanoparticles to the one-dimensional polymer
matrix gradually increased the removal rate of organic dyes due
to higher specic surface area and the positive form of titania at
the interface.
Conclusion
Owing to its many advantages mainly involving most stable and
active naturally occurring photocatalyst, TiO2 is, so for, seen as
the best catalytic material for degradation of various contaminants and sustainable environmental remediation technology.
It has been widely employed in dye photodegradation studies.
Photodegradation of industrial dyes using improved TiO2 has
presented a somewhat promising and effective treatment technology. However, in order to overcome constraint such as
sensitivity towards operational parameters i.e. pH, temperature,
catalyst dose, amount of dye, inability for high photon efficiency
This journal is © The Royal Society of Chemistry 2014
RSC Advances
to utilize wider solar spectra, and separation aer treatment
inhibits the ability of TiO2 from its real time application on a
vast scale. Therefore, more advanced level research studies are
needed to address TiO2 shortfalls or to formulate potential
alternative for TiO2.
Acknowledgements
The authors of this work acknowledge the nancial support
from Department of Environmental Sciences, Quaid-i-Azam
University, Islamabad and Higher Education Commission of
Pakistan.
Notes and references
1 R. J. Fessenden and J. S. Fessenden, Adv. Drug Res., 1967, 4,
95–132.
2 H. Park and W. Choi, J. Photochem. Photobiol., A, 2003, 159,
241–247.
3 I. A. Alaton, I. A. Balcioglu and D. W. Bahnemann, Water
Res., 2002, 36, 1143–1154.
4 U. Pagga and D. Brown, Chemosphere, 1986, 15, 479–491.
5 N. Bensalah, M. Alfaro and C. Martı́nez-Huitle, Chem. Eng.
J., 2009, 149, 348–352.
6 K. Turhan and Z. Turgut, Desalination, 2009, 242, 256–263.
7 F. Gosetti, V. Gianotti, S. Angioi, S. Polati, E. Marengo and
M. C. Gennaro, J. Chromatogr. A, 2004, 1054, 379–387.
8 A. Houas, H. Lachheb, M. Ksibi, E. Elaloui, C. Guillard and
J.-M. Herrmann, Appl. Catal., B, 2001, 31, 145–157.
9 H. Zollinger, Color chemistry: syntheses, properties, and
applications of organic dyes and pigments, Wiley-VCH, 2003.
10 W. S. Perkins, Textile Chemist and Colorist and American
Dyestuff Reporter, 1999, vol. 1, pp. 33–37.
11 I. K. Konstantinou and T. A. Albanis, Appl. Catal., B, 2004,
49, 1–14.
12 R. Kant, Nat. Sci., 2012, 04, 22–26.
13 R. Anliker, Ecotoxicol. Environ. Saf., 1979, 3, 59–74.
14 J. Shore, Indian Journal of Fiber and Textile Research, 1996,
21, 1–29.
15 C. Carliell, S. Barclay and C. Buckley, Water SA, 1996, 22,
225–233.
16 N. Willmott, J. Guthrie and G. Nelson, J. Soc. Dyers Colour.,
1998, 114, 38–41.
17 G. Mishra and M. Tripathy, Colourage, 1993, 40, 35.
18 M. Senthilkumar and M. Muthukumar, Dyes Pigm., 2007,
72, 251–255.
19 R. Leena and S. Raj, Afr. J. Biotechnol., 2008, 71(8), 3309–
3313.
20 G. L. Baughman and T. A. Perenich, Environ. Toxicol. Chem.,
1988, 7, 183–199.
21 K.-T. Chung, G. E. Fulk and M. Egan, Appl. Environ.
Microbiol., 1978, 35, 558–562.
22 E. J. Weber and R. L. Adams, Environ. Sci. Technol., 1995, 29,
1163–1170.
23 U. Bali, E. Catalkaya and F. Sengul, J. Hazard. Mater., 2004,
114, 159–166.
24 M. Rauf and S. S. Ashraf, Chem. Eng. J., 2009, 151, 10–18.
RSC Adv., 2014, 4, 37003–37026 | 37019
View Article Online
Published on 05 August 2014. Downloaded by University of Birmingham on 26/08/2014 06:04:41.
RSC Advances
25 N. Daneshvar, M. Rasoulifard, A. Khataee and
F. Hosseinzadeh, J. Hazard. Mater., 2007, 143, 95–101.
26 T. Robinson, G. McMullan, R. Marchant and P. Nigam,
Bioresour. Technol., 2001, 77, 247–255.
27 A. G. Prado, L. B. Bolzon, C. P. Pedroso, A. O. Moura and
L. L. Costa, Appl. Catal., B, 2008, 82, 219–224.
28 A. Cassano, R. Molinari, M. Romano and E. Drioli, J. Membr.
Sci., 2001, 181, 111–126.
29 G. Crini, Bioresour. Technol., 2006, 97, 1061–1085.
30 M. Perez-Urquiza and J. Beltran, J. Chromatogr. A, 2000, 898,
271–275.
31 F. Hueber-Becker, G. J. Nohynek, E. K. Dufour,
W. J. Meuling, A. T. H. de Bie, H. Toutain and H. M. Bolt,
Food Chem. Toxicol., 2007, 45, 160–169.
32 D. Wróbel, A. Boguta and R. M. Ion, J. Photochem. Photobiol.,
A, 2001, 138, 7–22.
33 L. Yang, Y. Lin, J. Jia, X. Xiao, X. Li and X. Zhou, J. Power
Sources, 2008, 182, 370–376.
34 N. I. Georgiev, V. B. Bojinov and P. S. Nikolov, Dyes Pigm.,
2009, 81, 18–26.
35 R. Nilsson, R. Nordlinder, U. Wass, B. Meding and L. Belin,
Br. J. Ind. Med., 1993, 50, 65–70.
36 W. Walthall and J. Stark, Environ. Pollut., 1999, 104, 207–215.
37 S. Tsuda, M. Murakami, N. Matsusaka, K. Kano,
K. Taniguchi and Y. F. Sasaki, Toxicol. Sci., 2001, 61, 92–99.
38 C. Zaharia and D. Suteu, Adsorption of cationic dye on
cellolignin, BioResources, 2012, 8(1), 427–446.
39 A. Price, A. C. Cohen and I. Johnson, J.J. Pizzuto's fabric
science, Fairchild Publications, New York, 8th edn, 2005.
40 R. M. Christie, Colour chemistry, Royal Society of Chemistry,
2001.
41 B. P. Corbman and M. D. Potter, Textiles: Fiber to Fabric,
McGraw-Hill New York, NY, USA, 1975.
42 A. Datyner, Rev. Prog. Color. Relat. Top., 1993, 23, 40–50.
43 C. Stead, Dyes Pigm., 1982, 3, 161–171.
44 V. Golob and A. Ojstršek, Dyes Pigm., 2005, 64, 57–61.
45 P. E. McGovern and R. H. Michel, Acc. Chem. Res., 1990, 23,
152–158.
46 H. L. Needles, Handbook of textile bers, dyes and nishes,
Garland STPM Press, 1981.
47 W. Z. Tang and A. Huren, Chemosphere, 1995, 31, 4157–
4170.
48 M. A. Brown and S. C. De Vito, Crit. Rev. Environ. Sci.
Technol., 1993, 23, 249–324.
49 Y. M. Slokar and A. Majcen Le Marechal, Dyes Pigm., 1998,
37, 335–356.
50 M. Sleiman, D. Vildozo, C. Ferronato and J.-M. Chovelon,
Appl. Catal., B, 2007, 77, 1–11.
51 W. Kuo, Water Res., 1992, 26, 881–886.
52 N. Ince and D. Gönenç, Environ. Technol., 1997, 18, 179–185.
53 O. Tünay, I. Kabdasli, G. Eremektar and D. Orhon, Water
Sci. Technol., 1996, 34, 9–16.
54 M. Saquib and M. Muneer, Dyes Pigm., 2003, 56, 37–49.
55 E. P. Reddy, L. Davydov and P. Smirniotis, Appl. Catal., B,
2003, 42, 1–11.
56 O. J. Hao, H. Kim and P.-C. Chiang, Crit. Rev. Environ. Sci.
Technol., 2000, 30, 449–505.
37020 | RSC Adv., 2014, 4, 37003–37026
Review
57 A. Moutaouakkil, Y. Zeroual, F. Zohra Dzayri, M. Talbi,
K. Lee and M. Blaghen, Arch. Biochem. Biophys., 2003, 413,
139–146.
58 C. Shaw, C. Carliell and A. Wheatley, Water Res., 2002, 36,
1993–2001.
59 G. M. Bonser, L. Bradshaw, D. Clayson and J. Jull, Br. J.
Cancer, 1956, 10, 539.
60 I. Arslan and I. A. Balcioğlu, Dyes Pigm., 1999, 43, 95–108.
61 K. Kunitou, S. Maeda, S. Hongyou and K. Mishima, Can. J.
Chem. Eng., 2002, 80, 208–213.
62 S. Chakrabarti and B. K. Dutta, J. Hazard. Mater., 2004, 112,
269–278.
63 J. Sun, X. Wang, J. Sun, R. Sun, S. Sun and L. Qiao, J. Mol.
Catal. A: Chem., 2006, 260, 241–246.
64 J. Madhavan, P. Maruthamuthu, S. Murugesan and
S. Anandan, Appl. Catal., B, 2008, 83, 8–14.
65 X.-H. Qi, Y.-Y. Zhuang, Y.-C. Yuan and W.-X. Gu, J. Hazard.
Mater., 2002, 90, 51–62.
66 P. Pizarro, C. Guillard, N. Perol and J.-M. Herrmann, Catal.
Today, 2005, 101, 211–218.
67 H. Yates, M. Nolan, D. Sheel and M. Pemble, J. Photochem.
Photobiol., A, 2006, 179, 213–223.
68 M. Ni, M. K. Leung, D. Y. Leung and K. Sumathy, Renewable
Sustainable Energy Rev., 2007, 11, 401–425.
69 L.-C. Chen and T.-C. Chou, Ind. Eng. Chem. Res., 1994, 33,
1436–1443.
70 G. Annadurai, T. Sivakumar and S. R. Babu, Bioprocess Eng.,
2000, 23, 167–173.
71 W. A. Sadik, A. W. Nashed and A.-G. M. El-Demerdash, J.
Photochem. Photobiol., A, 2007, 189, 135–140.
72 Y. Jiang, Y. Sun, H. Liu, F. Zhu and H. Yin, Dyes Pigm., 2008,
78, 77–83.
73 E. Bizani, K. Fytianos, I. Poulios and V. Tsiridis, J. Hazard.
Mater., 2006, 136, 85–94.
74 K. Vinodgopal and P. V. Kamat, Environ. Sci. Technol., 1995,
29, 841–845.
75 C. Chen, X. Li, W. Ma, J. Zhao, H. Hidaka and N. Serpone, J.
Phys. Chem. B, 2002, 106, 318–324.
76 K. Vinodgopal, D. E. Wynkoop and P. V. Kamat, Environ. Sci.
Technol., 1996, 30, 1660–1666.
77 U. G. Akpan and B. H. Hameed, J. Hazard. Mater., 2009, 170,
520–529.
78 W. Tang, Z. Zhang, H. An, M. Quintana and D. Torres,
Environ. Technol., 1997, 18, 1–12.
79 X. Li and F. Li, Environ. Sci. Technol., 2001, 35, 2381–2387.
80 Y. Wang, Water Res., 2000, 34, 990–994.
81 M. Stylidi, D. I. Kondarides and X. E. Verykios, Appl. Catal.,
B, 2003, 40, 271–286.
82 K. Tanaka, K. Padermpole and T. Hisanaga, Water Res.,
2000, 34, 327–333.
83 H. Lachheb, E. Puzenat, A. Houas, M. Ksibi, E. Elaloui,
C. Guillard and J.-M. Herrmann, Appl. Catal., B, 2002, 39,
75–90.
84 C. A. K. Gouvêa, F. Wypych, S. G. Moraes, N. Durán,
N. Nagata and P. Peralta-Zamora, Chemosphere, 2000, 40,
433–440.
This journal is © The Royal Society of Chemistry 2014
View Article Online
Published on 05 August 2014. Downloaded by University of Birmingham on 26/08/2014 06:04:41.
Review
85 A. Bianco Prevot, C. Baiocchi, M. C. Brussino, E. Pramauro,
P. Savarino, V. Augugliaro, G. Marcı̀ and L. Palmisano,
Environ. Sci. Technol., 2001, 35, 971–976.
86 F. Zhang, J. Zhao, T. Shen, H. Hidaka, E. Pelizzetti and
N. Serpone, Appl. Catal., B, 1998, 15, 147–156.
87 J. Zhao, T. Wu, K. Wu, K. Oikawa, H. Hidaka and
N. Serpone, Environ. Sci. Technol., 1998, 32, 2394–2400.
88 J. T. Spadaro, L. Isabelle and V. Renganathan, Environ. Sci.
Technol., 1994, 28, 1389–1393.
89 B. Neppolian, H. C. Choi, S. Sakthivel, B. Arabindoo and
V. Murugesan, Chemosphere, 2002, 46, 1173–1181.
90 S. Sakthivel, B. Neppolian, M. V. Shankar, B. Arabindoo,
M. Palanichamy and V. Murugesan, Sol. Energy Mater. Sol.
Cells, 2003, 77, 65–82.
91 C. M. So, M. Y. Cheng, J. C. Yu and P. K. Wong,
Chemosphere, 2002, 46, 905–912.
92 C. Hu, J. C. Yu, Z. Hao and P. K. Wong, Appl. Catal., B, 2003,
42, 47–55.
93 C. Minero, V. Maurino and E. Pelizzetti, Res. Chem.
Intermed., 1997, 23, 291–310.
94 H. Chun and W. Yizhong, Chemosphere, 1999, 39, 2107–
2115.
95 V. Augugliaro, C. Baiocchi, A. Bianco Prevot, E. Garcı́aLópez, V. Loddo, S. Malato, G. Marcı́, L. Palmisano,
M. Pazzi and E. Pramauro, Chemosphere, 2002, 49, 1223–
1230.
96 K. Nohara, H. Hidaka, E. Pelizzetti and N. Serpone, J.
Photochem. Photobiol., A, 1997, 102, 265–272.
97 V. Maurino, C. Minero, E. Pelizzetti, P. Piccinini, N. Serpone
and H. Hidaka, J. Photochem. Photobiol., A, 1997, 109, 171–
176.
98 M. Abdullah, G. K. C. Low and R. W. Matthews, J. Phys.
Chem., 1990, 94, 6820–6825.
99 M. Kerzhentsev, C. Guillard, J.-M. Herrmann and P. Pichat,
Catal. Today, 1996, 27, 215–220.
100 K. Pirkanniemi and M. Sillanpää, Chemosphere, 2002, 48,
1047–1060.
101 M. Stylidi, D. I. Kondarides and X. E. Verykios, Appl. Catal.,
B, 2004, 47, 189–201.
102 S. Kaur and V. Singh, J. Hazard. Mater., 2007, 141, 230–236.
103 C. Kormann, D. Bahnemann and M. R. Hoffmann, Environ.
Sci. Technol., 1991, 25, 494–500.
104 W. Liu, S. Chen, W. Zhao and S. Zhang, Desalination, 2009,
249, 1288–1293.
105 J. M. Peralta-Hernández, Y. Meas-Vong, F. J. Rodrı́guez,
T. W. Chapman, M. I. Maldonado and L. A. Godı́nez,
Water Res., 2006, 40, 1754–1762.
106 S. Lakshmi, R. Renganathan and S. Fujita, J. Photochem.
Photobiol., A, 1995, 88, 163–167.
107 D. C. Hurum, A. G. Agrios, K. A. Gray, T. Rajh and
M. C. Thurnauer, J. Phys. Chem. B, 2003, 107, 4545–4549.
108 H. Yin, Y. Wada, T. Kitamura, S. Kambe, S. Murasawa,
H. Mori, T. Sakata and S. Yanagida, J. Mater. Chem., 2001,
11, 1694–1703.
109 A. Riga, K. Soutsas, K. Ntampegliotis, V. Karayannis and
G. Papapolymerou, Desalination, 2007, 211, 72–86.
This journal is © The Royal Society of Chemistry 2014
RSC Advances
110 V. K. Gupta, R. Jain, A. Nayak, S. Agarwal and
M. Shrivastava, Mater. Sci. Eng., C, 2011, 31, 1062–1067.
111 M. A. Nadeem, K. A. Connelly and H. Idriss, Int. J.
Nanotechnol., 2012, 9, 121–162.
112 A. Shiga, A. Tsujiko, S. Yae and Y. Nakato, Bull. Chem. Soc.
Jpn., 1998, 71, 2119–2125.
113 G. Riegel and J. R. Bolton, J. Phys. Chem., 1995, 99, 4215–
4224.
114 M. Abdullah, G. K. Low and R. W. Matthews, J. Phys. Chem.,
1990, 94, 6820–6825.
115 Z. Zhang, W. Wang, M. Shang and W. Yin, J. Hazard. Mater.,
2010, 177, 1013–1018.
116 L. F. Velasco, J. B. Parra and C. O. Ania, Appl. Surf. Sci., 2010,
256, 5254–5258.
117 A. Khataee, M. Fathinia, S. Aber and M. Zarei, J. Hazard.
Mater., 2010, 181, 886–897.
118 S. Sreekantan and L. C. Wei, J. Alloys Compd., 2010, 490,
436–442.
119 H.-F. Yu and S.-T. Yang, J. Alloys Compd., 2010, 492, 695–
700.
120 K. Naeem and F. Ouyang, Phys. B, 2010, 405, 221–226.
121 M. A. Fox and M. T. Dulay, Chem. Rev., 1993, 93, 341–357.
122 M. R. Hoffmann, S. T. Martin, W. Choi and
D. W. Bahnemann, Chem. Rev., 1995, 95, 69–96.
123 J. Peral, X. Domènech and D. F. Ollis, J. Chem. Technol.
Biotechnol., 1997, 70, 117–140.
124 J. Saien and A. R. Soleymani, J. Ind. Eng. Chem., 2012, 18,
1683–1688.
125 J. Zhao, C. Chen and W. Ma, Top. Catal., 2005, 35, 269–
278.
126 C. Galindo, P. Jacques and A. Kalt, J. Photochem. Photobiol.,
A, 2000, 130, 35–47.
127 Y. Ma and J.-n. Yao, J. Photochem. Photobiol., A, 1998, 116,
167–170.
128 F. Chen, Y. Xie, J. Zhao and G. Lu, Chemosphere, 2001, 44,
1159–1168.
129 F. Zhang, J. Zhao, T. Shen, H. Hidaka, E. Pelizzetti and
N. Serpone, Appl. Catal., B, 1998, 15, 147–156.
130 H. Zhu, R. Jiang, Y. Fu, Y. Guan, J. Yao, L. Xiao and G. Zeng,
Desalination, 2012, 286, 41–48.
131 M. Behnajady, N. Modirshahla and R. Hamzavi, J. Hazard.
Mater., 2006, 133, 226–232.
132 S. K. Kansal, M. Singh and D. Sud, J. Hazard. Mater., 2008,
153, 412–417.
133 M. Muruganandham and M. Swaminathan, Sol. Energy
Mater. Sol. Cells, 2004, 81, 439–457.
134 S. Sakthivel, B. Neppolian, M. Shankar, B. Arabindoo,
M. Palanichamy and V. Murugesan, Sol. Energy Mater. Sol.
Cells, 2003, 77, 65–82.
135 M. Qamar, M. Saquib and M. Muneer, Dyes Pigm., 2005, 65,
1–9.
136 S. Tunesi and M. Anderson, J. Phys. Chem., 1991, 95, 3399–
3405.
137 M. S. Goncalves, A. M. Oliveira-Campos, E. M. Pinto,
P. Plasência and M. J. R. Queiroz, Chemosphere, 1999, 39,
781–786.
RSC Adv., 2014, 4, 37003–37026 | 37021
View Article Online
Published on 05 August 2014. Downloaded by University of Birmingham on 26/08/2014 06:04:41.
RSC Advances
138 A. H. Mahvi, M. Ghanbarian, S. Nasseri and A. Khairi,
Desalination, 2009, 239, 309–316.
139 W. Baran, A. Makowski and W. Wardas, Chemosphere, 2003,
53, 87–95.
140 W. Z. Tang and R. Z. Chen, Chemosphere, 1996, 32, 947–958.
141 B. Neppolian, H. Choi, S. Sakthivel, B. Arabindoo and
V. Murugesan, Chemosphere, 2002, 46, 1173–1181.
142 E. Bizani, K. Fytianos, I. Poulios and V. Tsiridis, J. Hazard.
Mater., 2006, 136, 85–94.
143 J. Wiszniowski, D. Robert, J. Surmacz-Gorska, K. Miksch
and J.-V. Weber, J. Photochem. Photobiol., A, 2002, 152,
267–273.
144 C. Raillard, V. Héquet, P. Le Cloirec and J. Legrand, Water
Sci. Technol., 2004, 50, 241–250.
145 D. Hufschmidt, D. Bahnemann, J. J. Testa, C. A. Emilio and
M. I. Litter, J. Photochem. Photobiol., A, 2002, 148, 223–231.
146 M. Vautier, J. Catal., 2001, 201, 46–59.
147 I. Poulios and I. Tsachpinis, J. Chem. Technol. Biotechnol.,
1999, 74, 349–357.
148 I. Poulios, A. Avranas, E. Rekliti and A. Zouboulis, J. Chem.
Technol. Biotechnol., 2000, 75, 205–212.
149 L. B. Reutergådh and M. Iangphasuk, Chemosphere, 1997,
35, 585–596.
150 D. Curcó, J. Gimenez, A. Addardak, S. Cervera-March and
S. Esplugas, Catal. Today, 2002, 76, 177–188.
151 M. Qamar, M. Muneer and D. Bahnemann, J. Environ.
Manage., 2006, 80, 99–106.
152 C. Karunakaran and S. Senthilvelan, Catal. Commun., 2005,
6, 159–165.
153 G. C. Collazzo, E. L. Foletto, S. L. Jahn and M. A. Villetti, J.
Environ. Manage., 2012, 98, 107–111.
154 N. San, A. Hatipoǧlu, G. Koçtürk and Z. Çınar, J. Photochem.
Photobiol., A, 2001, 139, 225–232.
155 C. A. Gouvea, F. Wypych, S. G. Moraes, N. Duran, N. Nagata
and P. Peralta-Zamora, Chemosphere, 2000, 40, 433–440.
156 M. Saquib and M. Muneer, Dyes Pigm., 2002, 53, 237–249.
157 A. F. Caliman, C. Cojocaru, A. Antoniadis and I. Poulios, J.
Hazard. Mater., 2007, 144, 265–273.
158 J. Percherancier, R. Chapelon and B. Pouyet, J. Photochem.
Photobiol., A, 1995, 87, 261–266.
159 A. B. Prevot, M. Vincenti, B. A. and E. Pramauro, Appl.
Catal., B, 1999, 22, 149–158.
160 I. Poulios and I. Aetopoulou, Environ. Technol., 1999, 20,
479–487.
161 R. W. Matthews, Sol. Energy, 1987, 38, 405–413.
162 M. Saquib, T. M. Abu, M. Haque and M. Muneer, J. Environ.
Manage., 2008, 88, 300.
163 C. Lung-Chyuan and C. Tse-Chuan, J. Mol. Catal., 1993, 85,
201–214.
164 E. C. Ilinoiu, R. Pode, F. Manea, L. A. Colar, A. Jakab,
C. Orha, C. Ratiu, C. Lazau and P. Sfarloaga, J. Taiwan
Inst. Chem. Eng., 2012, 44(2), 270–278.
165 H. Wang, C. Xie, W. Zhang, S. Cai, Z. Yang and Y. Gui, J.
Hazard. Mater., 2007, 141, 645–652.
166 M. N. Chong, B. Jin, C. W. Chow and C. Saint, Water Res.,
2010, 44, 2997–3027.
37022 | RSC Adv., 2014, 4, 37003–37026
Review
167 C.-H. Liao, S.-F. Kang and F.-A. Wu, Chemosphere, 2001, 44,
1193–1200.
168 X. Wang, J. Jia and Y. Wang, J. Hazard. Mater., 2011, 185,
315–321.
169 H. Zhu, J.-Y. Li, J.-C. Zhao and G. J. Churchman, Appl. Clay
Sci., 2005, 28, 79–88.
170 A. Aguedach, S. Brosillon, J. Morvan and K. Lhadi El, J.
Hazard. Mater., 2008, 150, 250–256.
171 U. Diebold, Surf. Sci. Rep., 2003, 48, 53–229.
172 X. Chen, W. Wang, H. Xiao, C. Hong, F. Zhu, Y. Yao and
Z. Xue, Chem. Eng. J., 2012, 193–194, 290–295.
173 R. Venkatadri and R. W. Peters, Hazard. Waste Hazard.
Mater., 1993, 10, 107–149.
174 J. Fernandez, J. Bandara, A. Lopez, P. Buffat and J. Kiwi,
Langmuir, 1999, 15, 185–192.
175 M. R. Dhananjeyan, E. Mielczarski, K. R. Thampi, P. Buffat,
M. Bensimon, A. Kulik, J. Mielczarski and J. Kiwi, J. Phys.
Chem. B, 2001, 105, 12046–12055.
176 A. Bozzi, M. Dhananjeyan, I. Guasaquillo, S. Parra,
C. Pulgarin, C. Weins and J. Kiwi, J. Photochem. Photobiol.,
A, 2004, 162, 179–185.
177 S. S. Reddy and B. Kotaiah, Int. J. Environ. Sci. Technol.,
2005, 2, 245–251.
178 X. Wang, Z. Yao, J. Wang, W. Guo and G. Li, Ultrason.
Sonochem., 2008, 15, 43–48.
179 I. K. Kim and C. P. Huang, J. Chin. Inst. Eng., 2005, 28, 1107–
1118.
180 R. Mettin, S. Luther, C.-D. Ohl and W. Lauterborn, Ultrason.
Sonochem., 1999, 6, 25–29.
181 T. Leighton, Ultrason. Sonochem., 1995, 2, S123–S136.
182 S. Tangestaninejad, M. Moghadam, V. Mirkhani,
I. Mohammadpoor-Baltork and H. Salavati, Ultrason.
Sonochem., 2008, 15, 815–822.
183 I. Z. Shirgaonkar and A. B. Pandit, Ultrason. Sonochem.,
1998, 5, 53–61.
184 N. L. Stock, J. Peller, K. Vinodgopal and P. V. Kamat,
Environ. Sci. Technol., 2000, 34, 1747–1750.
185 M. Mrowetz, C. Pirola and E. Selli, Ultrason. Sonochem.,
2003, 10, 247–254.
186 K. M. Kalumuck and G. L. Chahine, http://
resolver.caltech.edu/cav2001:sessionA4.006, 2001.
187 M. Sivakumar and A. B. Pandit, Ultrason. Sonochem., 2002,
9, 123–131.
188 P. R. Gogate and A. B. Pandit, Adv. Environ. Res., 2004, 8,
501–551.
189 V. K. Saharan, A. B. Pandit, P. S. Satish Kumar and
S. Anandan, Ind. Eng. Chem. Res., 2011, 51, 1981–1989.
190 Y. Deng and C. M. Ezyske, Water Res., 2011, 45, 6189–6194.
191 P. Nfodzo and H. Choi, Chem. Eng. J., 2011, 174, 629–634.
192 J. Criquet and N. K. V. Leitner, Chemosphere, 2009, 77, 194–
200.
193 R. H. Waldemer, P. G. Tratnyek, R. L. Johnson and
J. T. Nurmi, Environ. Sci. Technol., 2007, 41, 1010–1015.
194 P. Neta, V. Madhavan, H. Zemel and R. W. Fessenden, J. Am.
Chem. Soc., 1977, 99, 163–164.
195 G. P. Anipsitakis and D. D. Dionysiou, Environ. Sci. Technol.,
2004, 38, 3705–3712.
This journal is © The Royal Society of Chemistry 2014
View Article Online
Published on 05 August 2014. Downloaded by University of Birmingham on 26/08/2014 06:04:41.
Review
196 K. B. Dhanalakshmi, S. Anandan, J. Madhavan and
P. Maruthamuthu, Sol. Energy Mater. Sol. Cells, 2008, 92,
457–463.
197 A. Zaleska, Recent Pat. Eng., 2008, 2, 157–164.
198 J. Zhang, Y. Wu, M. Xing, S. A. K. Leghari and S. Sajjad,
Energy Environ. Sci., 2010, 3, 715–726.
199 C. Ying, D. Hao and W. Lishi, J. Mater. Sci. Technol., 2008,
24, 675–689.
200 M. Fittipaldi, V. Gombac, A. Gasparotto, C. Deiana,
G. Adami, D. Barreca, T. Montini, G. Martra, D. Gatteschi
and P. Fornasiero, ChemPhysChem, 2011, 12, 2221–2224.
201 D. Chen, Z. Jiang, J. Geng, Q. Wang and D. Yang, Ind. Eng.
Chem. Res., 2007, 46, 2741–2746.
202 Y. Zhang, H. Xu, Y. Xu, H. Zhang and Y. Wang, J. Photochem.
Photobiol., A, 2005, 170, 279–285.
203 W. Balcerski, S. Y. Ryu and M. R. Hoffmann, J. Phys. Chem.
C, 2007, 111, 15357–15362.
204 T. Tachikawa, Y. Takai, S. Tojo, M. Fujitsuka, H. Irie,
K. Hashimoto and T. Majima, J. Phys. Chem. B, 2006, 110,
13158–13165.
205 D. Meroni, S. Ardizzone, G. Cappelletti, C. Oliva, M. Ceotto,
D. Poelman and H. Poelman, Catal. Today, 2011, 161, 169–
174.
206 A. Emeline, X. Zhang, M. Jin, T. Murakami and
A. Fujishima, J. Photochem. Photobiol., A, 2009, 207, 13–19.
207 B. Wawrzyniak and A. W. Morawski, Appl. Catal., B, 2006,
62, 150–158.
208 Y. Cong, J. Zhang, F. Chen and M. Anpo, J. Phys. Chem. C,
2007, 111, 6976–6982.
209 A. R. Gandhe, S. P. Naik and J. B. Fernandes, Microporous
Mesoporous Mater., 2005, 87, 103–109.
210 Z. He and H. He, Appl. Surf. Sci., 2011, 258, 972–976.
211 C. Wang, M. Wang, K. Xie, Q. Wu, L. Sun, Z. Lin and C. Lin,
Nanotechnology, 2011, 22, 305607.
212 F. Peng, L. Cai, H. Yu, H. Wang and J. Yang, J. Solid State
Chem., 2008, 181, 130–136.
213 X. Chen, Y. B. Lou, A. C. Samia, C. Burda and J. L. Gole, Adv.
Funct. Mater., 2005, 15, 41–49.
214 N. Sobana and M. Swaminathan, Sol. Energy Mater. Sol.
Cells, 2007, 91, 727–734.
215 Y. J. Jang, C. Simer and T. Ohm, Mater. Res. Bull., 2006, 41,
67–77.
216 R. Asahi, T. Morikawa, T. Ohwaki, K. Aoki and Y. Taga,
science, 2001, 293, 269–271.
217 C. Di Valentin, E. Finazzi, G. Pacchioni, A. Selloni,
S. Livraghi, M. C. Paganini and E. Giamello, Chem. Phys.,
2007, 339, 44–56.
218 H. Irie, Y. Watanabe and K. Hashimoto, J. Phys. Chem. B,
2003, 107, 5483–5486.
219 K. Parida and B. Naik, J. Colloid Interface Sci., 2009, 333,
269–276.
220 A. Selvaraj, S. Sivakumar, A. Ramasamy and
V. Balasubramanian, Res. Chem. Intermed., 2013, 39,
2287–2302.
221 T. Ihara, M. Miyoshi, Y. Iriyama, O. Matsumoto and
S. Sugihara, Appl. Catal., B, 2003, 42, 403–409.
222 N. Serpone, J. Phys. Chem. B, 2006, 110, 24287–24293.
This journal is © The Royal Society of Chemistry 2014
RSC Advances
223 P. Songkhum and J. Tantirungrotechai, Res. Chem.
Intermed., 2013, 39, 1555–1561.
224 J. Sun, L. Qiao, S. Sun and G. Wang, J. Hazard. Mater., 2008,
155, 312–319.
225 B. Neumann, P. Bogdanoff, H. Tributsch, S. Sakthivel and
H. Kisch, J. Phys. Chem. B, 2005, 109, 16579–16586.
226 S. U. Khan, M. Al-Shahry and W. B. Ingler, science, 2002,
297, 2243–2245.
227 S. Sakthivel and H. Kisch, Angew. Chem., Int. Ed., 2003, 42,
4908–4911.
228 W. Ren, Z. Aia, F. Jiaa, L. Zhanga, X. Fanb and Z. Zoub, Appl.
Catal., B, 2007, 69, 138–144.
229 R. Velmurugan, B. Krishnakumar, B. Subash and
M. Swaminathan, Sol. Energy Mater. Sol. Cells, 2013, 108,
205–212.
230 K. Ranjit, I. Willner, S. Bossmann and A. Braun, Environ.
Sci. Technol., 2001, 35, 1544–1549.
231 A.-W. Xu, Y. Gao and H.-Q. Liu, J. Catal., 2002, 207, 151–157.
232 D. W. Hwang, J. S. Lee, W. Li and S. H. Oh, J. Phys. Chem. B,
2003, 107, 4963–4970.
233 S. Matsuo, N. Sakaguchi, K. Yamada, T. Matsuo and
H. Wakita, Appl. Surf. Sci., 2004, 228, 233–244.
234 Y. Wang, H. Cheng, L. Zhang, Y. Hao, J. Ma, B. Xu and
W. Li, J. Mol. Catal. A: Chem., 2000, 151, 205–216.
235 Y. Zhang, H. Zhang, Y. Xu and Y. Wang, J. Solid State Chem.,
2004, 177, 3490–3498.
236 X. Zhang, M. Zhou and L. Lei, Carbon, 2005, 43, 1700–
1708.
237 Y. Xie, C. Yuan and X. Li, Colloids Surf., A, 2005, 252, 87–94.
238 Y. Xie, C. Yuan and X. Li, Mater. Sci. Eng., B, 2005, 117, 325–
333.
239 W. Zhang, X. Li, G. Jia, Y. Gao, H. Wang, Z. Cao, C. Li and
J. Liu, Catal. Commun., 2014, 45, 144–147.
240 X. Lan, L. Wang, B. Zhang, B. Tian and J. Zhang, Catal.
Today, 2014, 224, 163–170.
241 M. Nasir, J. Zhang, F. Chen and B. Tian, Res. Chem.
Intermed., 2013, 1–18.
242 M. Nasir, Z. Xi, M. Xing, J. Zhang, F. Chen, B. Tian and
S. Bagwasi, J. Phys. Chem. C, 2013, 117, 9520–9528.
243 T. Yu, X. Tan, L. Zhao, Y. Yin, P. Chen and J. Wei, Chem.
Eng. J., 2010, 157, 86–92.
244 W. Choi, A. Termin and M. R. Hoffmann, J. Phys. Chem.,
1994, 98, 13669–13679.
245 L. Andronic, A. Enesca, C. Vladuta and A. Duta, Chem. Eng.
J., 2009, 152, 64–71.
246 X. S. Li, G. E. Fryxell, M. H. Engelhard and C. Wang, Inorg.
Chem. Commun., 2007, 10, 639–641.
247 H. Chun, T. Yuchao and T. Hongxiao, Catal. Today, 2004,
90, 325–330.
248 M. Di Paola, P. Zaccagnino, G. Montedoro, T. Cocco and
M. Lorusso, J. Bioenerg. Biomembr., 2004, 36, 165–170.
249 I. H. Tseng, J. C. S. Wu and H.-Y. Chou, J. Catal., 2004, 221,
432–440.
250 F. Zhuge, X. Li, X. Gao, X. Gan and F. Zhou, Mater. Lett.,
2009, 63, 652–654.
251 A. A. Sagade and R. Sharma, Sens. Actuators, B, 2008, 133,
135–143.
RSC Adv., 2014, 4, 37003–37026 | 37023
View Article Online
Published on 05 August 2014. Downloaded by University of Birmingham on 26/08/2014 06:04:41.
RSC Advances
252 L. Andronic, L. Isac and A. Duta, J. Photochem. Photobiol., A,
2011, 221, 30–37.
253 L. Huang, F. Peng, H. Yu and H. Wang, Solid State Sci.,
2009, 11, 129–138.
254 F. Sayilkan, M. Asilturk, P. Tatar, N. Kiraz, E. Arpac and
H. Sayilkan, J. Hazard. Mater., 2007, 144, 140–146.
255 M. K. Seery, R. George, P. Floris and S. C. Pillai, J.
Photochem. Photobiol., A, 2007, 189, 258–263.
256 M. V. Liga, E. L. Bryant, V. L. Colvin and Q. Li, Water Res.,
2011, 45, 535–544.
257 C. Sun, Q. Li, S. Gao, L. Cao and J. K. Shang, J. Am. Ceram.
Soc., 2010, 93, 3880–3885.
258 P. Wu, R. Xie, K. Imlay and J. K. Shang, Environ. Sci.
Technol., 2010, 44, 6992–6997.
259 A. L. Linsebigler, G. Lu and J. T. Yates Jr, Chem. Rev., 1995,
95, 735–758.
260 D. Behar and J. Rabani, J. Phys. Chem. B, 2006, 110, 8750–
8755.
261 X. You, F. Chen, J. Zhang and M. Anpo, Catal. Lett., 2005,
102, 247–250.
262 A. Gupta, A. Pal and C. Sahoo, Dyes Pigm., 2006, 69, 224–
232.
263 C. Gunawan, W. Y. Teoh, C. P. Marquis, J. Lia and R. Amal,
Small, 2009, 5, 341–344.
264 S. T. Hussain, Rashid, D. Anjum, A. Siddiqa and
A. Badshah, Mater. Res. Bull., 2013, 48, 705–714.
265 S. Sato, J. M. White and T. U. A. A. D. O. CHEMISTRY,
Photodecomposition of Water Over Pt/TiO2 Catalysts,
Defense Technical Information Center, 1980.
266 S. Sato and J. White, J. Phys. Chem., 1981, 85, 592–594.
267 I. Izumi, F.-R. F. Fan and A. J. Bard, J. Phys. Chem., 1981, 85,
218–223.
268 M. S. John, A. Furgala and A. Sammells, J. Electrochem. Soc.,
1982, 129, 246–250.
269 H. Einaga, M. Harada, S. Futamura and T. Ibusuki, J. Phys.
Chem. B, 2003, 107, 9290–9297.
270 Y. Gai, J. Li, S.-S. Li, J.-B. Xia and S.-H. Wei, Phys. Rev. Lett.,
2009, 102, 036402.
271 T. Ohno, Z. Miyamoto, K. Nishijima, H. Kanemitsu and
F. Xueyuan, Appl. Catal., A, 2006, 302, 62–68.
272 M. Y. Xing, D. Y. Qi, J. L. Zhang and F. Chen, Chem.–Eur. J.,
2011, 17, 11432–11436.
273 F. Yang, H. Yang, B. Tian, J. Zhang and D. He, Res. Chem.
Intermed., 2013, 39, 1685–1699.
274 L. Yan, Y. Cheng, S. Yuan, X. Yan, X. Hu and K. Oh, Res.
Chem. Intermed., 2013, 39, 1673–1684.
275 U. G. Akpan and B. H. Hameed, Chem. Eng. J., 2011, 169, 91–
99.
276 M. Zhang, C. Chen, W. Ma and J. Zhao, Angew. Chem., 2008,
120, 9876–9879.
277 H. Zhang, R. Zong, J. Zhao and Y. Zhu, Environ. Sci.
Technol., 2008, 42, 3803–3807.
278 H.-c. Liang and X.-z. Li, Appl. Catal., B, 2009, 86, 8–17.
279 A. E. Regazzoni, P. Mandelbaum, M. Matsuyoshi,
S. Schiller, S. A. Bilmes and M. A. Blesa, Langmuir, 1998,
14, 868–874.
37024 | RSC Adv., 2014, 4, 37003–37026
Review
280 J. Moser, S. Punchihewa, P. P. Infelta and M. Graetzel,
Langmuir, 1991, 7, 3012–3018.
281 S. Ikeda, C. Abe, T. Torimoto and B. Ohtani, J. Photochem.
Photobiol., A, 2003, 160, 61–67.
282 B. Zhang, W. Zou and J. Zhang, Res. Chem. Intermed., 2010,
1–14.
283 A. Di Paola, E. Garcia-Lopez, G. Marci and L. Palmisano, J.
Hazard. Mater., 2012, 211–212, 3–29.
284 G. K. Mor, O. K. Varghese, M. Paulose, K. Shankar and
C. A. Grimes, Sol. Energy Mater. Sol. Cells, 2006, 90, 2011–
2075.
285 H.-F. Zhuang, C.-J. Lin, Y.-K. Lai, L. Sun and J. Li, Environ.
Sci. Technol., 2007, 41, 4735–4740.
286 L. K. Tan, M. K. Kumar, W. W. An and H. Gao, ACS Appl.
Mater. Interfaces, 2010, 2, 498–503.
287 J. Toledo Antonio, M. Cortes-Jacome, S. Orozco-Cerros,
E. Montiel-Palacios, R. Suarez-Parra, C. Angeles-Chavez,
J. Navarete and E. López-Salinas, Appl. Catal., B, 2010,
100, 47–54.
288 H. Xu, G. Vanamu, Z. Nie, H. Konishi, R. Yeredla, J. Phillips
and Y. Wang, J. Nanomater., 2006, 2006, 23.
289 J. M. Macak, M. Zlamal, J. Krysa and P. Schmuki, Small,
2007, 3, 300–304.
290 Y. Lai, L. Sun, Y. Chen, H. Zhuang, C. Lin and J. W. Chin, J.
Electrochem. Soc., 2006, 153, D123–D127.
291 Y. Wang, R. Shi, J. Lin and Y. Zhu, Appl. Catal., B, 2010, 100,
179–183.
292 M. Ishigami, J. Chen, W. Cullen, M. Fuhrer and
E. Williams, Nano Lett., 2007, 7, 1643–1648.
293 H. Zhang, X. Lv, Y. Li, Y. Wang and J. Li, ACS Nano, 2009, 4,
380–386.
294 B. Qiu, M. Xing and J. Zhang, J. Am. Chem. Soc., 2014, 136,
5852–5855.
295 V. Krishna, N. Noguchi, B. Koopman and B. Moudgil, J.
Colloid Interface Sci., 2006, 304, 166–171.
296 W.-C. Oh, A.-R. Jung and W.-B. Ko, J. Ind. Eng. Chem., 2007,
13, 1208–1214.
297 S. Mu, Y. Long, S.-Z. Kang and J. Mu, Catal. Commun., 2010,
11, 741–744.
298 H. G. Yang, G. Liu, S. Z. Qiao, C. H. Sun, Y. G. Jin,
S. C. Smith, J. Zou, H. M. Cheng and G. Q. Lu, J. Am.
Chem. Soc., 2009, 131, 4078–4083.
299 J. S. Chen, Y. L. Tan, C. M. Li, Y. L. Cheah, D. Luan,
S. Madhavi, F. Y. C. Boey, L. A. Archer and X. W. Lou, J.
Am. Chem. Soc., 2010, 132, 6124–6130.
300 S. Liu, J. Yu and M. Jaroniec, J. Am. Chem. Soc., 2010, 132,
11914–11916.
301 H. Yu, B. Tian and J. Zhang, Chem.–Eur. J., 2011, 17, 5499–
5502.
302 I. M. Arabatzis, S. Antonaraki, T. Stergiopoulos, A. Hiskia,
E. Papaconstantinou, M. C. Bernard and P. Falaras, J.
Photochem. Photobiol., A, 2002, 149, 237–245.
303 K. Kabra, R. Chaudhary and R. L. Sawhney, Ind. Eng. Chem.
Res., 2004, 43, 7683–7696.
304 N. Bao, X. Feng, Z. Yang, L. Shen and X. Lu, Environ. Sci.
Technol., 2004, 38, 2729–2736.
This journal is © The Royal Society of Chemistry 2014
View Article Online
Published on 05 August 2014. Downloaded by University of Birmingham on 26/08/2014 06:04:41.
Review
305 V. Loddo, G. Marci, L. Palmisano and A. Sclafani, Mater.
Chem. Phys., 1998, 53, 217–224.
306 Y. G. Adewuyi, Environ. Sci. Technol., 2005, 39, 8557–8570.
307 A. Masarwa, S. Rachmilovich-Calis, N. Meyerstein and
D. Meyerstein, Coord. Chem. Rev., 2005, 249, 1937–1943.
308 E. Chamarro, A. Marco and S. Esplugas, Water Res., 2001,
35, 1047–1051.
309 B. Mounir, M.-N. Pons, O. Zahraa, A. Yaacoubi and
A. Benhammou, J. Hazard. Mater., 2007, 148, 513–520.
310 S. Fukahori, H. Ichiura, T. Kitaoka and H. Tanaka, Environ.
Sci. Technol., 2003, 37, 1048–1051.
311 M. Karches, M. Morstein, P. Rudolf von Rohr, R. L. Pozzo,
J. L. Giombi and M. A. Baltanás, Catal. Today, 2002, 72,
267–279.
312 T.-H. Kim, C. Park and S. Kim, J. Cleaner Prod., 2005, 13,
779–786.
313 M. A. Behnajady, N. Modirshahla, M. Shokri, H. Elham and
A. Zeininezhad, J. Environ. Sci. Health, Part A: Toxic/Hazard.
Subst. Environ. Eng., 2008, 43, 460–467.
314 Y. M. Xu, P. E. Ménassa and C. H. Langford, Chemosphere,
1988, 17, 1971–1976.
315 A. Y. Shan, T. I. M. Ghazi and S. A. Rashid, Appl. Catal., A,
2010, 389, 1–8.
316 C.-H. Huang, K.-P. Chang, H.-D. Ou, Y.-C. Chiang,
E.-E. Chang and C.-F. Wang, J. Hazard. Mater., 2011, 186,
1174–1182.
317 C.-C. Wang, C.-K. Lee, M.-D. Lyu and L.-C. Juang, Dyes
Pigm., 2008, 76, 817–824.
318 M. Nikazar, K. Gholivand and K. Mahanpoor, Desalination,
2008, 219, 293–300.
319 H. Zhu, R. Jiang, L. Xiao, Y. Chang, Y. Guan, X. Li and
G. Zeng, J. Hazard. Mater., 2009, 169, 933–940.
320 L. Rizzo, J. Koch, V. Belgiorno and M. A. Anderson,
Desalination, 2007, 211, 1–9.
321 H. Zhang and L. Yang, Thin Solid Films, 2012, 520, 5922–5927.
322 M. A. Behnajady, N. Modirshahla, N. Daneshvar and
M. Rabbani, Chem. Eng. J., 2007, 127, 167–176.
323 R. W. Matthews, Water Res., 1991, 25, 1169–1176.
324 O. Carp, C. L. Huisman and A. Reller, Prog. Solid State
Chem., 2004, 32, 33–177.
325 R. W. Matthews, J. Catal., 1988, 111, 264–272.
326 Y. Kuwahara, T. Kamegawa, K. Mori and H. Yamashita,
Chem. Commun., 2008, 2008, 4783–4785.
327 N. O. Gopal, H.-H. Lo and S.-C. Ke, J. Am. Chem. Soc., 2008,
130, 2760–2761.
328 M. Xing, D. Qi, J. Zhang, F. Chen, B. Tian, S. Bagwas and
M. Anpo, J. Catal., 2012, 294, 37–46.
329 M. Xing, W. Fang, M. Nasir, Y. Ma, J. Zhang and M. Anpo, J.
Catal., 2013, 297, 236–243.
330 D. Qi, M. Xing and J. Zhang, J. Phys. Chem. C, 2014, 118,
7329–7336.
331 G. A. Roberts, Chitin chemistry, Macmillan, 1992.
332 M. N. Ravi Kumar, React. Funct. Polym., 2000, 46, 1–27.
333 I. Aranaz, M. Mengı́bar, R. Harris, I. Paños, B. Miralles,
N. Acosta, G. Galed and Á Heras, Curr. Chem. Biol., 2009,
3, 203–230.
334 W. Ngah and S. Fatinathan, Chem. Eng. J., 2008, 143, 62–72.
This journal is © The Royal Society of Chemistry 2014
RSC Advances
335 D. Chauhan and N. Sankararamakrishnan, Bioresour.
Technol., 2008, 99, 9021–9024.
336 A.-H. Chen, S.-C. Liu, C.-Y. Chen and C.-Y. Chen, J. Hazard.
Mater., 2008, 154, 184–191.
337 C. E. Zubieta, P. V. Messina, C. Luengo, M. Dennehy,
O. Pieroni and P. C. Schulz, J. Hazard. Mater., 2008, 152,
765–777.
338 Z. Zainal, L. K. Hui, M. Z. Hussein, A. H. Abdullah and
I. R. Hamadneh, J. Hazard. Mater., 2009, 164, 138–145.
339 R. Jiang, H. Zhu, X. Li and L. Xiao, Chem. Eng. J., 2009, 152,
537–542.
340 X. Wang, Y. Du, S. Ding, L. Fan, X. Shi, Q. Wang and
G. Xiong, Phys. E, 2005, 30, 96–100.
341 R. Khan, A. Kaushik, P. R. Solanki, A. A. Ansari,
M. K. Pandey and B. Malhotra, Anal. Chim. Acta, 2008,
616, 207–213.
342 J.-Y. Chen, P.-J. Zhou, J.-L. Li and Y. Wang, Carbohydr.
Polym., 2008, 72, 128–132.
343 P. Serp, M. Corrias and P. Kalck, Appl. Catal., A, 2003, 253,
337–358.
344 M. M. Nassar and M. S. El-Geundi, J. Chem. Technol.
Biotechnol., 1991, 50, 257–264.
345 F. Rodriguez-Reinoso, Carbon, 1998, 36, 159–175.
346 G. Li Puma, A. Bono, D. Krishnaiah and J. G. Collin,
J. Hazard. Mater., 2008, 157, 209–219.
347 B. Tryba, Int. J. Photoenergy, 2008, 2008.
348 J. Matos, J. Laine and J.-M. Herrmann, J. Catal., 2001, 200,
10–20.
349 S. X. Liu, X. Y. Chen and X. Chen, J. Hazard. Mater., 2007,
143, 257–263.
350 Y. Ao, J. Xu, S. Zhang and D. Fu, Appl. Surf. Sci., 2010, 256,
2754–2758.
351 T. Cordero, J.-M. Chovelon, C. Duchamp, C. Ferronato and
J. Matos, Appl. Catal., B, 2007, 73, 227–235.
352 C. Raghavacharya, Chem. Eng. World, 1997, 32, 53–54.
353 J. Araña, J. Dona-Rodrıguez, E. Tello Rendón, C. Garriga i
Cabo, O. González-Dıaz, J. Herrera-Melián, J. Pérez-Peña,
G. Colón and J. Navı́o, Appl. Catal., B, 2003, 44, 153–
160.
354 X. Zhang, M. Zhou and L. Lei, Carbon, 2006, 44, 325–333.
355 D.-K. Lee, S.-C. Kim, S.-J. Kim, I.-S. Chung and S.-W. Kim,
Chem. Eng. J., 2004, 102, 93–98.
356 X. Ma, S. Wang, J. Gong, X. Yang and G. Xu, J. Mol. Catal. A:
Chem., 2004, 222, 183–187.
357 A. Fernandez, G. Lassaletta, V. Jimenez, A. Justo,
A. Gonzalez-Elipe, J.-M. Herrmann, H. Tahiri and Y. AitIchou, Appl. Catal., B, 1995, 7, 49–63.
358 P. Yuan, D. Wu, H. He and Z. Lin, Appl. Surf. Sci., 2004, 227,
30–39.
359 G. Tian, H. Fu, L. Jing, B. Xin and K. Pan, J. Phys. Chem. C,
2008, 112, 3083–3089.
360 J. Xu, Y. Ao, D. Fu and C. Yuan, J. Phys. Chem. Solids, 2008,
69, 2366–2370.
361 Z. Sun, C. Bai, S. Zheng, X. Yang and R. L. Frost, Appl.
Catal., A, 2013, 458, 103–110.
362 D. Eder, Chem. Rev., 2010, 110, 1348–1385.
RSC Adv., 2014, 4, 37003–37026 | 37025
View Article Online
Published on 05 August 2014. Downloaded by University of Birmingham on 26/08/2014 06:04:41.
RSC Advances
363 Y. Yu, J. C. Yu, J.-G. Yu, Y.-C. Kwok, Y.-K. Che, J.-C. Zhao,
L. Ding, W.-K. Ge and P.-K. Wong, Appl. Catal., A, 2005,
289, 186–196.
364 Q. Wang, D. Yang, D. Chen, Y. Wang and Z. Jiang, J.
Nanopart. Res., 2007, 9, 1087–1096.
365 W. Oh and M. Chen, Bull. Korean Chem. Soc., 2008, 29, 159.
366 H. Yu, X. Quan, S. Chen, H. Zhao and Y. Zhang, J.
Photochem. Photobiol., A, 2008, 200, 301–306.
367 Y. Yao, G. Li, S. Ciston, R. M. Lueptow and K. A. Gray,
Environ. Sci. Technol., 2008, 42, 4952–4957.
37026 | RSC Adv., 2014, 4, 37003–37026
Review
368 Y. Yu, J. C. Yu, C.-Y. Chan, Y.-K. Che, J.-C. Zhao, L. Ding,
W.-K. Ge and P.-K. Wong, Appl. Catal., B, 2005, 61, 1–11.
369 Y. Luo, J. Liu, X. Xia, X. Li, T. Fang, S. Li, Q. Ren, J. Li and
Z. Jia, Mater. Lett., 2007, 61, 2467–2472.
370 D. Chowdhury, A. Paul and A. Chattopadhyay, Langmuir,
2005, 21, 4123–4128.
371 Y. Cheng, L. An, F. Gao, G. Wang, X. Li and X. Chen, Res.
Chem. Intermed., 2013, 39, 3969–3979.
This journal is © The Royal Society of Chemistry 2014