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<Articles><Article><Journal><PublisherName></PublisherName><JournalTitle>Journal of Environmental Health Science &amp; Engineering</JournalTitle><Volume>8</Volume><Issue>2</Issue></Journal><ArticleTitle>REMOVAL OF DIVALENT NICKEL FROM AQUEOUS SOLUTIONS BY ADSORPTION ONTO MODIFIED HOLLY SAWDUST: EQUILIBRIUM AND KINETICS</ArticleTitle><FirstPage>167</FirstPage><LastPage>174</LastPage><AuthorList><Author><FirstName>M.</FirstName><LastName>Samarghandi</LastName></Author><Author><FirstName>S.</FirstName><LastName>Azizian</LastName></Author><Author><FirstName>M.</FirstName><LastName>Siboni</LastName></Author><Author><FirstName>S.</FirstName><LastName>Jafari</LastName></Author><Author><FirstName>S.</FirstName><LastName>Rahimi</LastName></Author></AuthorList><History><PubDate PubStatus="received"><Year>2015</Year><Month>12</Month><Day>09</Day></PubDate></History><Abstract>The removal of divalent nickel from aqueous solutions on modified 
holly sawdust was studied at varying contact times, pH, initial divalent
 nickel concentrations and adsorbent dose. Results showed the removal 
efficiency by increasing of pH increased and decreased with initial 
nickel divalent concentration. By increasing pH from 2 to 12 
(equilibrium time= 240 min, adsorbent dose= 0.6g/100 mL, divalent nickel
 concentrations= 60 mg/L), the removal efficiency increased from 17.47 %
 to 81.76 %. Also removal efficiency was decreased from 98 % to 19.3 % 
by increasing of initial divalent nickel concentrations from 20 mg/l to 
100 mg/L. Also the results showed the removal efficiency was increased 
by increasing of adsorbent dose and contact time. By increasing of 
adsorbent dose from 0.2 g/100CC to 1 g/100CC, the removal efficiency 
increased from 32.78% to 99.98%. The removal efficiency increased from 
34.7% to 83.67% by increasing of contact time from 5 min to 240 min. 
Experimental equilibrium and kinetics data were fitted by Langmuir and 
Freundlich isotherms and pseudo-first-order and pseudo-second-order 
kinetics models, respectively. The results show that the equilibrium 
data follow Langmuir isotherm and the kinetic data follow 
pseudo-second-order model. The obtained maximum adsorption capacity was 
22.47 mg/g at a pH 7. The results show that the modified holly sawdust 
can be used for the treatment of aqueous solutions containing nickel as a
 low cost adsorbent.</Abstract><web_url>https://ijehse.tums.ac.ir/index.php/jehse/article/view/290</web_url><pdf_url>https://ijehse.tums.ac.ir/index.php/jehse/article/download/290/289</pdf_url></Article><Article><Journal><PublisherName></PublisherName><JournalTitle>Journal of Environmental Health Science &amp; Engineering</JournalTitle><Volume>8</Volume><Issue>2</Issue></Journal><ArticleTitle>APPLICATION OF NANOFILTRATION MEMBRANE IN THE SEPARATION OF AMOXICILLIN FROM PHARMACEUTICAL WASTEWATER</ArticleTitle><FirstPage>106</FirstPage><LastPage>110</LastPage><AuthorList><Author><FirstName>A.</FirstName><LastName>Shahtalebi</LastName></Author><Author><FirstName>M.</FirstName><LastName>Sarrafzadeh</LastName></Author></AuthorList><History><PubDate PubStatus="received"><Year>2015</Year><Month>12</Month><Day>09</Day></PubDate></History><Abstract>Separation of amoxicillin from pharmaceutical wastewater by 
nanofiltration (NF) membrane has been investigated in this study. For 
this purpose a membrane system including a polyamide spiral wound NF 
membrane was evaluated for the treatment of amoxicillin wastewater. The 
effects of operating conditions such as flow rate, pressure and 
concentration of amoxicillin and COD in the feed, on the efficiency of 
the membrane were evaluated. The permeation flux and rejection of 
amoxicillin and COD were the criteria for this evaluation. The rejection
 of the amoxicillin by the selected NF membrane was adequate and in most
 cases exceeded 97% whereas COD reached a maximum of 40% rejection and 
permeation flux was over 1.5 L/min.m2. The rise in pressure 
enhanced the transport rate of the solvents. Permeation flux of the NF 
membrane increased with increasing flow rates. Experimental data also 
indicated that concentration polarization existed in this membrane 
separation process. The stable permeation flux and high rejection of 
amoxicillin indicated the potential of NF for the recovery of 
amoxicillin from the pharmaceutical wastewater</Abstract><web_url>https://ijehse.tums.ac.ir/index.php/jehse/article/view/291</web_url><pdf_url>https://ijehse.tums.ac.ir/index.php/jehse/article/download/291/290</pdf_url></Article><Article><Journal><PublisherName></PublisherName><JournalTitle>Journal of Environmental Health Science &amp; Engineering</JournalTitle><Volume>8</Volume><Issue>2</Issue></Journal><ArticleTitle>A COMPARATIVE STUDY ON ARSENIC (III) REMOVAL FROM AQUEOUS SOLUTION USING NANO AND MICRO SIZED ZERO-VALENT IRON</ArticleTitle><FirstPage>157</FirstPage><LastPage>166</LastPage><AuthorList><Author><FirstName>A.</FirstName><LastName>Rahmani</LastName></Author><Author><FirstName>H.</FirstName><LastName>Ghaffari</LastName></Author><Author><FirstName>M.</FirstName><LastName>Samadi</LastName></Author></AuthorList><History><PubDate PubStatus="received"><Year>2015</Year><Month>12</Month><Day>09</Day></PubDate></History><Abstract>The present study was conducted for Arsenic (III) removal, one of the
 most poisonous groundwater pollutants, by synthetic nano and micro size
 zerovalent iron (n-mZVI). Batch experiments were performed to 
investigate the influence of As (III), nZVI and mZVI concentration, pH 
of solution and reaction time on the efficiency of As (III) removal by 
Fe0 particles. Nano ZVI was synthesized by reduction of ferric chloride 
by sodium borohydrid. Scanning Electron microscope and X-Ray diffraction
 were used to determine particle size and characterization of produced 
nanoparticles. Results showed up to 99.9% removal efficiency for arsenic
 (III) that was obtained by nZVI dosage of 1 g/L at equal time of 10 min
 and pH=7. The maximum removal efficiency by mZVI obtained in initial 
arsenic concentration of 1 mg/L and mZVI dosage of 10 g/L after 120 min.
 and pH=7. It could be concluded that the removal efficiency was 
enhanced with increasing n-mZVI dosage and reaction time, but decreased 
with increasing of arsenic concentration and pH for both nano and micro 
sized ZVI. Nano ZVI presented an outstanding ability to remove As (III) 
due to not only a high surface area and low particle size but also to 
high inherent activity.</Abstract><web_url>https://ijehse.tums.ac.ir/index.php/jehse/article/view/292</web_url><pdf_url>https://ijehse.tums.ac.ir/index.php/jehse/article/download/292/291</pdf_url></Article><Article><Journal><PublisherName></PublisherName><JournalTitle>Journal of Environmental Health Science &amp; Engineering</JournalTitle><Volume>8</Volume><Issue>2</Issue></Journal><ArticleTitle>EFFECT OF FENTON PROCESS (H2O2 / FE2+) ON REMOVAL OF LINEAR ALKYLBENZENE SULFONATE (LAS) USING CENTERAL COMPOSITE DESIGN AND RESPONSE SURFACE METHODOLOGY</ArticleTitle><FirstPage>111</FirstPage><LastPage>116</LastPage><AuthorList><Author><FirstName>S. A.</FirstName><LastName>Mousavi</LastName></Author><Author><FirstName>A.</FirstName><LastName>Mahvi</LastName></Author><Author><FirstName>S.</FirstName><LastName>Nasseri</LastName></Author><Author><FirstName>Sh.</FirstName><LastName>Ghaffari</LastName></Author></AuthorList><History><PubDate PubStatus="received"><Year>2015</Year><Month>12</Month><Day>09</Day></PubDate></History><Abstract>This study investigates the degradation of Linear Alkylbenzene 
Sulfonate (LAS) in aqueous solution using Fenton's process in a batch 
reactor (at pH = 3 and 25&amp;deg;C). Experiments were carried out to survey the
 effects of the amounts of ferrous sulfate (FeSO4.7H2O) and hydrogen 
peroxide (H2O2) on the LAS and COD removal. Central composite design and
 response surface methods were used to optimize the Fenton oxidation 
process through examination of three independent operating variables 
namely oxidant dose (H2O2), catalyst dose (Fe+2) and reaction time., 
hydrogen peroxide dose ranging from 150 to 750 mg /L and Fe+2 
concentration in the range of 10 -130 mg /L were selected to be examined
 at different reaction times between 20 and 80 minutes. Models were 
developed and results shows that the oxidation capacities of H2O2 /Fe+2 
were highly dependent on the concentration of H2O2 and Fe+2. 
Satisfactory decay rates of LAS to lock up biodegradable concentration 
level were obtained, and in the case for oxidation of 200 mg /L LAS, the
 optimum values were achieved at 600 and 130 mg/L for H2O2 and Fe+2, 
respectively.</Abstract><web_url>https://ijehse.tums.ac.ir/index.php/jehse/article/view/293</web_url><pdf_url>https://ijehse.tums.ac.ir/index.php/jehse/article/download/293/292</pdf_url></Article><Article><Journal><PublisherName></PublisherName><JournalTitle>Journal of Environmental Health Science &amp; Engineering</JournalTitle><Volume>8</Volume><Issue>2</Issue></Journal><ArticleTitle>APPLICATION OF FLAT PLATE SOLAR COLLECTOR FOR THERMAL DISINFECTION OF WASTEWATER EFFLUENTS</ArticleTitle><FirstPage>121</FirstPage><LastPage>126</LastPage><AuthorList><Author><FirstName>D.</FirstName><LastName>Rabbani</LastName></Author><Author><FirstName>H.</FirstName><LastName>Hooshyar</LastName></Author></AuthorList><History><PubDate PubStatus="received"><Year>2015</Year><Month>12</Month><Day>09</Day></PubDate></History><Abstract>Application of solar energy for wastewater treatment has shown to 
have the least negative effects and costs. This experimental research 
was carried out in pilot-scale on the effluent of the extended aeration 
activated sludge wastewater treatment system in Kashan. The plant is 
located at the Kashan University of Medical Sciences campus and receives
 about 100 m3/d sewage from official and residential building blocks. In
 this study thermal disinfection of the effluent in 55 &amp;ordm;C for 2 hours 
using flat plat solar collector (FPSC) was investigated. During the 
study in the beginning of every week, one day was selected randomly and 
the pilot was run. The pilot influent temperature was the same as 
ambient air throughout the day. If the liquid temperature within the 
pilot increased above 55 &amp;ordm;C, a thermostatic valve opened. Passed liquid 
was maintained for 2 hours in this temperature. Whenever the volume of 
disinfected effluent was measurable fecal MPN test and Nemathoda eggs 
count-up were done according to the Standard Methods and Leeds-II 
directions, respectively. In 200 days from April to November the 
geometric mean of fecal coliform never exceeded the WHO guideline (1000 
MPN/100mL), but in 5 days (21% ) it exceeded the Iranian standard 
(400/100mL). Mathematical mean of Nemathoda eggs was less than 1 per 
liter (Engelberg Index) persistently. The mean of hydraulic loading 
rates was calculated 83.25 L/d m2 while it decreased to 41.85L/d.m2 in 
the days without thermal reclamation.</Abstract><web_url>https://ijehse.tums.ac.ir/index.php/jehse/article/view/294</web_url><pdf_url>https://ijehse.tums.ac.ir/index.php/jehse/article/download/294/293</pdf_url></Article><Article><Journal><PublisherName></PublisherName><JournalTitle>Journal of Environmental Health Science &amp; Engineering</JournalTitle><Volume>8</Volume><Issue>2</Issue></Journal><ArticleTitle>INTERACTION OF ACRYLONITRILE VAPORS ON A BENCH SCALE BIOFILTER TREATING STYRENE-POLLUTED WASTE GAS STREAMS</ArticleTitle><FirstPage>127</FirstPage><LastPage>132</LastPage><AuthorList><Author><FirstName>R.</FirstName><LastName>Dehghanzadeh</LastName></Author><Author><FirstName>H.</FirstName><LastName>Aslani</LastName></Author><Author><FirstName>A.</FirstName><LastName>Torkian</LastName></Author><Author><FirstName>M.</FirstName><LastName>Asadi</LastName></Author></AuthorList><History><PubDate PubStatus="received"><Year>2015</Year><Month>12</Month><Day>09</Day></PubDate></History><Abstract>Considering concurrent use of styrene and acrylonitrile as raw 
materials in the production of synthetic resins and plastic and their 
associated differences in physiochemical properties and 
biodegradability, our experiments were conducted in a three-stage 
downflow bench-scale biofilter to study the potential suppressive 
effects of acrylonitrile on styrene removal. A Mixture of yard waste 
compost and shredded plastics and activated sludge was used as bed 
media. Gas phase concentration of styrene and acrylonitrile was 
determined via gas chromatographic analysis. Under steady-state 
conditions, maximum elimination capacity of styrene and acrylonitrile 
was 44 and 120 g/m3 h, respectively. The effect of moisture was very 
significant in reducing the specific adsorptive capacity (&amp;mu;g/g of bed 
media) of styrene and acrylonitrile. The bed media with 60% moisture 
content lost styrene absorption capacities by more than one order of 
magnitude when compared to dry media. The existence of water increased 
the absorption capacity of medium for acrylonitrile about 95%. Styrene 
elimination capacity of the biofilter during co-treatment was less as 
compared to pure styrene biodegradation indicating the likelihood of 
inhibitory kinetics. Introduction of acrylonitrile into the air stream 
reduced elimination capacity of styrene to 103 g/m3 h. The adverse 
impact on removal rate of acrylonitrile due to the presence of styrene 
in the gas stream was minimal. Carbon-equivalent removal for the system 
amounted to about 85 g C/m3 h at empty bed retention time of 120 s.</Abstract><web_url>https://ijehse.tums.ac.ir/index.php/jehse/article/view/295</web_url><pdf_url>https://ijehse.tums.ac.ir/index.php/jehse/article/download/295/294</pdf_url></Article><Article><Journal><PublisherName></PublisherName><JournalTitle>Journal of Environmental Health Science &amp; Engineering</JournalTitle><Volume>8</Volume><Issue>2</Issue></Journal><ArticleTitle>BIOSORPTION OF Cr (VI) BY RESTING CELLS OF FUSARIUM SOLANI</ArticleTitle><FirstPage>117</FirstPage><LastPage>120</LastPage><AuthorList><Author><FirstName>M.</FirstName><LastName>Sen</LastName></Author></AuthorList><History><PubDate PubStatus="received"><Year>2015</Year><Month>12</Month><Day>09</Day></PubDate></History><Abstract>Chromium is one of the toxic heavy metals which exists in nature as 
stable hexavalent and trivalent forms. The hexavalent form of chromium 
is more toxic than trivalent chromium as it persists indefinitely in the
 environment complicating its remediation. The conventional physical and
 chemical treatment techniques used for the removal of Cr(VI) are 
expensive and highly energy intensive, moreover they produce harmful 
by-products, ultimate disposal of which again causes secondary 
pollution. Removal of Cr(VI) from aqueous solution using biological 
sources as biosorbent has assumed advantageous over the existing 
conventional physico-chemical techniques for the treatment of metal 
contaminated wastes. The present batch biosorption study was undertaken 
with an aim to examine the Cr (VI) removal potential of the resting 
cells of Fusarium solani (isolated from soil) from aqueous solution. The
 specific Cr (VI) removal decreased with increase in pH and increased 
with increase in initial Cr(VI) concentration , up to 500 mg/L . The 
specific Cr(VI) removal remained almost constant by increasing biomass 
concentration from 2.4 to 5.2 g/L. The studies also carried out by using
 the resting cells obtained from various stages of growth and the 
maximum specific Cr(VI) removal (60 mg/g ) was achieved at 500 mg/L 
initial Cr(VI) concentration and by using cells (36 h old). The Langmuir
 adsorption isotherm constants, Q0 and b were observed to be 57.1 mg/L 
and 0.06 l 1/mg, respectively.</Abstract><web_url>https://ijehse.tums.ac.ir/index.php/jehse/article/view/296</web_url><pdf_url>https://ijehse.tums.ac.ir/index.php/jehse/article/download/296/295</pdf_url></Article><Article><Journal><PublisherName></PublisherName><JournalTitle>Journal of Environmental Health Science &amp; Engineering</JournalTitle><Volume>8</Volume><Issue>2</Issue></Journal><ArticleTitle>OCCURRENCE OF AFLATOXIN M1 IN RAW MILK PRODUCED IN ARDEBIL OF IRAN</ArticleTitle><FirstPage>133</FirstPage><LastPage>140</LastPage><AuthorList><Author><FirstName>A.</FirstName><LastName>Kamkar</LastName></Author><Author><FirstName>Gh.</FirstName><LastName>Jahed Khaniki</LastName></Author><Author><FirstName>S.</FirstName><LastName>Alavi</LastName></Author></AuthorList><History><PubDate PubStatus="received"><Year>2015</Year><Month>12</Month><Day>09</Day></PubDate></History><Abstract>Contamination of milk and dairy products to aflatoxin M1 is a risk for human and it can be a public heath concern. The aim of this study was to evaluate the presence of aflatoxin M1 in raw milk samples produced in Ardebil City (Iran) by ELISA (Enzyme Linked Immuno Sorbent Assay) technique. 122 samples of raw milk were collected from milk collecting centers and dairy plants in the region and aflatoxin M1 contamination was detected in all of milk samples. The mean concentration of aflatoxin M1 was 40.01ng/L and 14.75 percent of the samples had higher levels than the maximum recommended limits by ISIRI, European Community and Codex Alimentarius. With a view of the fact that milk is used by all the age groups including infants and children in the city of Ardebil, it is necessary to apply an ideal recommended limit to minimize the health hazard from aflatoxin M1 contamination in milk. Application of Good Agricultural Practices and Good Veterinary Practices by agriculture and also the Hazard Analysis and Critical Control Points (HACCP) system as a draft code of practice for preharvest and postharvest control of dairy cow's feed and in milk and dairy products processing is effective.</Abstract><web_url>https://ijehse.tums.ac.ir/index.php/jehse/article/view/297</web_url><pdf_url>https://ijehse.tums.ac.ir/index.php/jehse/article/download/297/296</pdf_url></Article><Article><Journal><PublisherName></PublisherName><JournalTitle>Journal of Environmental Health Science &amp; Engineering</JournalTitle><Volume>8</Volume><Issue>2</Issue></Journal><ArticleTitle>SIMULATION OF TEMPERATURE CHANGES IN IRAN UNDER THE ATMOSPHERE CARBON DIOXIDE DUPLICATION CONDITION</ArticleTitle><FirstPage>141</FirstPage><LastPage>146</LastPage><AuthorList><Author><FirstName>Gh.</FirstName><LastName>Roshan</LastName></Author><Author><FirstName>F.</FirstName><LastName>Khoshakh lagh</LastName></Author><Author><FirstName>Gh.</FirstName><LastName>Azizi</LastName></Author><Author><FirstName>H.</FirstName><LastName>Mohammadi</LastName></Author></AuthorList><History><PubDate PubStatus="received"><Year>2015</Year><Month>12</Month><Day>09</Day></PubDate></History><Abstract>The present research intends to show the effect of global warming on 
the trend and patterns of temperature in Iran. The study has been 
divided into two primary parts, the first of which is an analysis of the
 country's temperature trend using the following data measures: the 
minimum, maximum, and mean seasonal night temperature (the minimum 
temperature) components, the day temperature (the maximum temperature) 
component and the mean daily temperature component. This data is 
specific to the time frame 1951 to 2005 and it was obtained from 92 
synoptic and climatology stations around the country. The second part of
 this research involved simulating and forecasting the effects of global
 warming on temperature values under conditions in which greenhouse 
gases have increased. For analyzing these simulations and forecasts the 
MAGICC SCENGEN model was used and different climate change scenarios 
were taken into consideration. The results are quite interesting. In the
 analysis of the country's current temperature trend and in the 
forecasting's, specifically related to time, a significant temperature 
increase was observed during the summer months. Also, with regard to 
altitudinal levels, it was evident that stations at higher altitudes 
show a more significant increase in daily and mean daily temperatures. 
Taking into account the output mean of the different climate change 
scenarios, the temperature simulations show a 4.41&amp;deg; C increase in Iran's
 mean temperature by 2100. Most of these temperature increases would 
occur in the southern and eastern parts of Bushehr, certain coastal 
regions of the Persian Gulf, eastern and western parts of Fars, 
Kohgilooye, Boyerahmad, southern parts of Yazd, as well as southern and 
southeastern parts of Esfahan</Abstract><web_url>https://ijehse.tums.ac.ir/index.php/jehse/article/view/298</web_url><pdf_url>https://ijehse.tums.ac.ir/index.php/jehse/article/download/298/297</pdf_url></Article><Article><Journal><PublisherName></PublisherName><JournalTitle>Journal of Environmental Health Science &amp; Engineering</JournalTitle><Volume>8</Volume><Issue>2</Issue></Journal><ArticleTitle>EQUILIBRIUM AND KINETICS STUDY OF REACTIVE RED 123 DYE REMOVAL FROM AQUEOUS SOLUTION BY ADSORPTION ON EGGSHELL</ArticleTitle><FirstPage>101</FirstPage><LastPage>106</LastPage><AuthorList><Author><FirstName>M.</FirstName><LastName>Ehrampoush</LastName></Author><Author><FirstName>Gh.</FirstName><LastName>Ghanizadeh</LastName></Author><Author><FirstName>M.</FirstName><LastName>Ghaneian</LastName></Author></AuthorList><History><PubDate PubStatus="received"><Year>2015</Year><Month>12</Month><Day>09</Day></PubDate></History><Abstract>The aim of this study was to determine the equilibrium and kinetics 
adsorption of reactive red 123 dye (RR 123) from aqueous solution with 
chicken's eggshell as an adsorbent. The initial concentrations of 
reactive red 123 dye were selected in the range of 25 and 50 mg/L. The 
target adsorbent was prepared in laboratory conditions and pulverized by
 ASTM standard sieves. Measurement of the adsorbent surface area was 
carried out via Brunauer-Emmett-Teller isotherm. The experimental data 
were analyzed with Langmuir, Freundlich and Temkin isotherm models. The 
results showed that the calcium components were the main constituents of
 eggshell (around 95% Ca). The experimental adsorption isotherm was in 
good concordance with Langmuir and Freundlich models (R2&amp;gt;0.90) and 
based on the Langmuir isotherm the maximum amount of adsorption (qmax) 
was 1.26 mg/g. Increase of the eggshell dose and the solution 
temperature beyond 45◦C led to decrease of the adsorbed dye per mass 
unit of the adsorbent, but increase of the solution pH up to 9 led to 
improvement of dye adsorption. The kinetic studies revealed that the 
adsorption of reactive red 123 was rapid and complied with pseudo 
second-order kinetic (R2= 0.99), with the kinetic constant of 0.02 
g/mg.min.</Abstract><web_url>https://ijehse.tums.ac.ir/index.php/jehse/article/view/299</web_url><pdf_url>https://ijehse.tums.ac.ir/index.php/jehse/article/download/299/298</pdf_url></Article><Article><Journal><PublisherName></PublisherName><JournalTitle>Journal of Environmental Health Science &amp; Engineering</JournalTitle><Volume>8</Volume><Issue>2</Issue></Journal><ArticleTitle>THE EFFECT OF METAL OXIDES ON THE REFINERY EFFLUENT TREATMENT</ArticleTitle><FirstPage>147</FirstPage><LastPage>156</LastPage><AuthorList><Author><FirstName>G.</FirstName><LastName>Soltanian</LastName></Author><Author><FirstName>M.</FirstName><LastName>Behbahani</LastName></Author></AuthorList><History><PubDate PubStatus="received"><Year>2015</Year><Month>12</Month><Day>09</Day></PubDate></History><Abstract>Metal Oxides (Titania TiO2, and Calamine (ZNO)) have been used as 
tertiary treatment for Refinery Effluent treatment and wastewaters to 
comply with the regulatory discharge limits and to oxidize persistent 
compounds that had not been oxidized in the biological treatment. The 
wastewater was provided by the Bandar Abbas Refinery. Although BOD 
removal is high in this plant, a residual and persistent COD (Chemical 
Oxygen Demand), besides a somewhat high phenol content remains. Three 
catalysts were tested TiO2 (Aldrich), ZnO (Aldrich), and TiO2 (P25, 
Degussa) by the UV radiation, the third being the most active. The 
optimized conditions obtained with an experimental design were 3.0 (g/L)
 TiO2 and pH=6.3. The use of hydrogen peroxide (H2O2) showed no 
beneficial effect. Removal of 93% of phenols, 56% of dissolved organic 
carbon (DOC), and more than 50% of oil and grease (OG) were achieved in 
the catalytic process with UV radiation, improving the quality of the 
treated wastewater.</Abstract><web_url>https://ijehse.tums.ac.ir/index.php/jehse/article/view/300</web_url><pdf_url>https://ijehse.tums.ac.ir/index.php/jehse/article/download/300/299</pdf_url></Article></Articles>
