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Decolorization of Dye with Iron Oxide Catalysed Decomposition of Hydrogen Peroxide

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Tiêu đề Decolorization of dye with iron oxide catalysed decomposition of hydrogen peroxide
Tác giả Joonseon Jeong, Jeyong Yoon
Trường học Seoul National University
Chuyên ngành Chemical Engineering
Thể loại bachelor thesis
Thành phố Seoul
Định dạng
Số trang 6
Dung lượng 269,82 KB

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peroxide. FeOOH was selected as iron oxide. The effect of FeOOH concentration, H2O2 concentration, the presence of radical scavenger, and pH on the dye removal and the decomposition of hydrogen peroxide was investigated. The rate of H2O2 decomposition was obtained as a pseudo-first-order kinetics relative to FeOOH concentration. However, despite of the increased H2O2 decomposition rate, the dye removal rate was not proportional to FeOOH concentration because FeOOH surface plays a role of scavenging OH radical. The H2O2 decomposition by FeOOH at pH 7 was more significant than that at pH 3, suggesting the possibility for overcoming limitations of homogeneous Fenton reaction which occurs only in acidic condition. The mechanism for the dye removal under the iron oxide catalysed decomposition of hydrogen peroxide was suggested, based on the experimental results obtained in this study.

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Decolorization of Dye with Iron Oxide Catalysed Decomposition of Hydrogen Peroxide

Joonseon Jeong, Jeyong Yoon

School of Chemical Engineering, College of Engineering, Seoul National University, San 56-1, Shilim-Dong, Kwanak-Goo, Seoul, Korea (151-742)

ABSTRACT

This study describes the dye removal under the iron oxide(FeOOH) catalysed decomposition of hydrogen

peroxide FeOOH was selected as iron oxide The effect of FeOOH concentration, H 2 O 2 concentration, the

presence of radical scavenger, and pH on the dye removal and the decomposition of hydrogen peroxide was

investigated The rate of H 2 O 2 decomposition was obtained as a pseudo-first-order kinetics relative to FeOOH

concentration However, despite of the increased H 2 O 2 decomposition rate, the dye removal rate was not

proportional to FeOOH concentration because FeOOH surface plays a role of scavenging OH radical The H 2 O 2

decomposition by FeOOH at pH 7 was more significant than that at pH 3, suggesting the possibility for

overcoming limitations of homogeneous Fenton reaction which occurs only in acidic condition The mechanism

for the dye removal under the iron oxide catalysed decomposition of hydrogen peroxide was suggested, based on

the experimental results obtained in this study

KEYWORDS

FeOOH, hydrogen peroxide, dye, hydroxyl radical, decolorization

INTRODUCTION AOPs (Advanced Oxidation Processes) which generate hydroxyl radical (OH•) have been introduced to water

depending on the how to produce OH• Among these types, Fenton’s reagent, a mixture of ferrous iron and hydrogen peroxide, has been applied to treat a various wastewater and contaminated soils (Venkatadri and Peters, 1993) But it is effective only in acidic pH In addition, the process generates a lot of iron sludge which need further treatment Alternatively, a number of researchers investigated about hydrogen peroxide

decomposition and contaminant degradation by iron oxide catalysed reaction (Valentine et al., 1998; Watts et

al., 1993; Abbot et al., 1990) Iron oxides are abundant in natural water and known to effectively decompose

hydrogen peroxide for generating hydroxyl radicals Especially, it has the advantage which can operate in neutral pH condition We selected dye as a model compound in this study The treatment of dye wastewater is

one of the most urgent subjects in pollution control because of its resistance to biodegradation (Ganesh et al.,

MATERIALS AND METHODS All solutions were prepared with deionised/distilled water, treated with a Barnstead NANO pure system, and analytical reagent grade chemicals Hydrogen peroxide (30.0-35.5%) was obtained from the Junsei Chemical

Chemical Company Reactive Red 6 was obtained from Imperial Chemical Industries All solutions used in experiment were prepared from dilution of the stock solution The experiments were conducted in open batch

and pH was not further adjusted The pH variation during the reaction was <±0.1 pH unit The reactions were

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peroxide concentration was determined spectrophotometrically using TiⅣmethod (Eisenberg, 1943) The aqueous concentration of dye was determined by measuring the absorbance intensity at the maximum absorbance wavelength(528nm), the calibration curve was established by standard solution before every experiments UV/VIS spectrophotometric measurements were performed on the Hewlett-Packard Diode Array Spectrophotometer(HP 8452) The pH was measured by pH-meter (Orion 710A)

RESULT AND DISCUSSION

considered FeOOH(Goethite) was found to be the most reactive with hydrogen peroxide among three iron

oxides at neutral pH condition(data not shown) This fact has also been reported by Lin et al (1998) Hence,

separate test, it was confirmed that the dye removal by adsorption on iron oxide surface was negligible and also any significant photochemical reaction was not observed by natural light under our experimental condition

Hydrogen peroxide decomposition kinetics

-3.5

-3

-2.5

-2

-1.5

-1

-0.5

0

time (hr)

O2

O2

]0

iron oxide 0.1 g/L iron oxide 0.3 g/L iron oxide 0.5 g/L iron oxide 1 g/L

0 0.0005 0.001 0.0015 0.002 0.0025

iron oxide concentration (g/L)

-1 )

R 2 = 0.9945

decomposition for different concentrations of iron oxide as a function of iron oxide concentration

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Effect of FeOOH concentrations on dye removal

0

0.001

0.002

0.003

0.004

FeOOH concentration (g/L)

-1 )

0 0.01 0.02 0.03 0.04

FeOOH concentration (g/L)

O 2

Figure 3 Observed first-order rate constant for Figure 4 Relationship between dye removal dye removal as a function of FeOOH concentration efficiency and FeOOH concentration

Hydroxyl radical can be generated by the reaction between hydrogen peroxide and metal surface (Weiss et al.,

1934) Dye removal can occur as a result of the reaction between dye and hydroxyl radicals The dye removal was investigated as a function of FeOOH concentration

Under the assumption that OH radical is the only reactive species on dye removal in this system, dye removal can be described by

] [ ]

[

dye k dt

dye

d

obs

=

ss OH

dye

k = + •[ •]

concentration In contrast with the result of Figure 2, dye removal was not proportional to the FeOOH concentration Rather, the observed first order rate constant for dye removal was reduced in the presence of excess FeOOH (1.0 g/L) This phenomena can be rationalized from the assumption that some portions of OH radical which is generated as a result of the reaction between hydrogen peroxide and FeOOH is wasted, not to

be used for dye removal That is, produced OH radical can be scavenged by FeOOH itself The stoichiometric

efficiency (E) which Valentine et al.(1998) defined was presented as a function of FeOOH (equation (2))

Figure 4 show that E for dye removal is inversely proportional to the FeOOH concentration This fact confirms again that FeOOH can act as a OH radical scavenger

] [

] [

2

2O H

compound E

Effect of radical scavenger on H 2 O 2 decomposition and dye removal

(1988)), hydrogen peroxide decomposition and dye removal were investigated to examine the dye removal mechanism Figure 5 & 6 show the different effect of tert-butanol on hydrogen peroxide decomposition and dye removal The presence of tert-butanol caused only slight change of hydrogen peroxide decomposition, whereas 10 mM of tert-butanol completely stopped the dye removal These observations support the following explanations for hydrogen peroxide decomposition and dye removal

since the presence of OH radical scavenger has no significant effect on hydrogen peroxide decomposition One

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possible explanation is that most of the H2O2 decomposition only takes place by FeOOH surface catalysed reaction However, dye removal occurs mainly by the reaction with OH radicals since the dye removal is greatly affected by the presence of tert-butanol (Figure 6)

constants with OH radical and the concentration of its competing compounds for OH radical It is known that

the dye removal experiment under the pseudo steady state condition of OH radical(equation (1), data not

Buxton et al (1988)) The relative difference of the respective rate constant of reaction make a decision of OH

radical reaction pathway

0

5

10

15

20

25

time (hr)

H2

O2

no t-BuOH

0 20 40 60 80 100 120

time (hr)

decomposition

Effect of pH on H2O2 decomposition and dye removal

0

5

10

15

20

25

time (hr)

H2

O2

pH3 pH7 pH10

0 20 40 60 80 100 120

time (hr)

pH3 pH7 pH10

decomposition removal

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decomposition and dye removal are enhanced as pH increases The H2O2 decomposition and dye removal were significantly hindered at pH of 3 favorable for homogeneous Fenton reaction This is a clear evidence for

homogeneous Fenton reaction mechanism

Reaction Mechanism

decomposition in the presence of sand was suggested by Miller et al (1999)

No Reaction

Scavenged

H2O2/HO2 -t-BuOH Surface

⋅OH

-Surface Scavenging

≡Fe(II)

≡Fe(III)

reduced state

oxidized state

decomposition rate proportionally OH radicals are produced by reaction 2 and scavenged mainly by two reactions in this experimental condition (FeOOH reactions and tert-butanol reaction) Dye removal (reaction 6) is competitive reaction with reaction 5 & 7

CONCLUSION

The removal of dye (Reactive Red 6) in hydrogen peroxide/iron oxide (FeOOH) system was investigated We have following conclusions

The FeOOH had the best catalytic effect on hydrogen peroxide decomposition among three iron

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The hydrogen peroxide decomposition by FeOOH followed a first order reaction with the H2O2 and FeOOH concentration

This is because the FeOOH surface not only generates the hydroxyl radicals, but also act as OH radical scavenger

The presence of tert-butanol reduced the rate of dye removal significantly with no or slight effect on hydrogen peroxide decomposition

ACKNOWLEDGEMENT Financial aid from the Brain Korea 21 Program (the Ministry of Education) is gratefully acknowledged

REFERENCES Abbot J and Brown D.G (1990) Kinetics of Iron-Catalysed Decomposition of Hydrogen Peroxide in

Alkaline Solution, Int J Chem Kinetics, 22, 963-974

Buxton G V., Greenstock C L., Helman W P and Ross A B (1988) Critical review of rate constants for

reactions of hydrated electrons, hydrogen atoms, and hydroxyl radicals in aqueous solution J Phys

Chem Ref Data., 17, 513-886

Eisenberg G.M (1943) Colorimetric determination of hydrogen peroxide Ind Eng Chem Anal., 15(5),

327–328

Ganesh R and Boardman G.D and Michelsen D (1994) Fate of Azo Dyes in Sludge Wat Res., 28,

1367-1376

Lin S and Gurol M.D (1998) Catalytic Decomposition of Hydrogen Peroxide on Iron Oxide: Kinetics,

Mechanism, and Implications Environ Sci Technol., 32, 1417-1423

Contaminant Degradation in the Presence of Sand, Wat Res., 33(12), 2805-2816

Valentine R.L and Ann Wang H.C (1998) Iron Oxide Surface Catalysed Oxidation of Quinoline by

Hydrogen Peroxide J Envir Engrg., 124(1), 31-38

Venkatadri R and Peters R.W (1993) Chemical Oxidation Technologies: Ultraviolet Light/Hydrogen

Peroxide, Fenton’s Reagent, and Titanium Dioxide-Assisted Photocatalysis Hazard Waste Mater.,

10, 107-149

Watts R.J and Udell M.D and Monsen R.M (1993) Use of Iron Minerals in Optimizing the Peroxide

Treatment of Contaminated Soils Water Environ Res., 65(7), 839-844

Weiss J J and Haber F (1934) The catalytic decomposition of hydrogen peroxide by iron salts Proc Roy

Soc London, Ser A, 147, 332

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