MOHAMED SAAD BALA
KKE15010
Contents
1 • Introduction
2 • Problem Statement
3 • Objective of the research
4 • Scope of the study
5 • Littre Review
6 • Methodology
7 • Result Analysis
8 • Conclusion & Recommendation
9 • References
Introduction
Introduction
Nowadays modern societies have been consistently exposed to environmental pollution (e.g. due to toxic compounds);
due to by toxic compounds has been being gaining wider concern in modern developed society.
Generally, petroleum refineries generate these polluted wastewater containing contain approximately 150-250 mg/L
of Chemical Oxygen Demand (COD), 20-200 mg/L of phenol and 100-300 mg/L oil of (Al-Malack 2013).
There are many ways that can be used several applications to remove COD. In the current work, however, this
research will be focusing on using hydrogen peroxide to can reduce COD by direct oxidation (either complete or
partial) of wastewater components.
The performances of using use of iron-catalyzed H2O2 (i.e. Fenton's Reagent) and Al2(SO4)3 catalyzed H2O2 in
reducing the amount of COD are compared.
PROBLEM STATEMENT
Typical petrochemical effluents have significant concentrations of Elements such as suspended solids, organic matter, oil and
grease, sulphide, ammonia, phenols, benzene, hydrocarbons, and COD can be found in a typical petrochemical effluent (e.g.
wastewater), which would affect are very high which generated environmental pollutions by toxic compounds produced from
them( Fabio, Malamis, Katsou, & Vecchiato, 2013).
Industry wastewater is a serious problem as it is affecting the freshwater resources, human health, and agricultural productivity. The problem
is more critical in the civilian and industrial areas where rapid water quality deterioration has caused widespread water-borne diseases and
other recoverable damages to the environment.
Wastewater treatment is very general and being applied throughout the world. Efforts of reducing COD must be developed in order
to safeguard our environment. Here, this research Illustrates that reducing COD in petrochemical wastewater is an important
process where the increase of COD causes pollution in environmental.
Therefore, it is significant to reduce COD to keep a safe environment to beat this issue aqueous solutions of Fe(II)/H2O2 (also
known as the Fenton’s reagent), because it is was found to be environmentally safe, cost effective and easy to operate.
PROBLEMSTATEMENT
Objective of the research
Objective of the research
The aim of this research is to reduce COD in the petrochemical wastewater
by the activation of hydrogen peroxide using via two different reagents.
Scope of the study
Scope of the study
1. To determine the quality of petrochemical wastewater via parameters such as (COD, pH, and TSS)
contributed to petrochemical wastewater pollution.
2. To study the effects of different activation reagents (i.e. Fe2+, Al3+) used to treat the wastewater.
3. To compare several parameters to COD removals such as the effects of concentration/dosage of H2O2,
concentration, and dosages of Al2(SO4)3 and concentration and dosages of FeSO4 on the removal efficiency of
COD.
4. To compare percentage reduction of COD using Fe2+ and Al3+ as activation reagent.
Littre Review
Author Finding
Awaleh & Soubaneh 2014 The resulting flock with the adsorbed oil is then separated, followed by sludge thickening and sludge dewatering
Midhun et al. 2016 without coagulation/flocculation, sedimentation can remove only coarse suspended matter such as that observed this type of
sedimentation typically takes place in a reservoir or sedimentation/clarification tank at the beginning of the treatment process
Karadag et al. 2015 Adsorption occurs when the attractive forces at the carbon surface overcome the attractive forces of the liquid
Glaze et al. 1987 Advanced Oxidation Processes (AOPs) are, in a broad sense, are a set of chemical treatment procedures adopted to remove
organic (or inorganic) materials in wastewater via oxidation through reactions with hydroxyl radicals (·OH) .
Mota et al. 2009 There are many methods that can be used to reduce the of pollutants from effluents
Augusto & Miyamoto
2011
H2O2 is one of the most powerful oxidizers.
Augusto & Miyamoto2011 . Fenton's chemistry uses hydrogen peroxides (H2O2) and iron salts where the effectiveness of H2O2 is improved by iron through
the generation of highly reactive hydroxyl radicals
Sax & DiMento 1974 Parameter Limit of Effluent Standard A and B
Methodology
Methodology
In this study, in general, the equipment was used for experimental and analysis was (pH, digital reactor block
(DRB200), DR 2800 portable spectrophotometer, the vacuum pump (300) and All-glass filtration assembly).
PH meter
The Mettler Toledo pH meter was used to
measure the pH value of the wastewater
sample.
Mettler Toledo pH meter
Chemical Oxygen Demand (COD)
Chemical Oxygen Demand (COD) was is
analyzed by using the HACH Method.
• The removal efficiency (% Removal)
was calculated from the following
formula:
•
• % Removal =
Co _𝑐
𝑐o
×100
DR2800 Spectrophotometer.Digital Reactor Block (DRB200)
Total suspended solids (TSS)
vacuum pump (300) and All-glass filtration
assembly.
Suspended solid is analyzed by using gravimetric method (APHA, 1985).
The TSS in the wastewater samples were calculated using the following
formula equations
g
mL
TSS =
WB _WA
Sample volume,mL
× 100
The removal efficiency (% Removal) was calculated from the following
formula:
% Removal =
TSSo _TSSt
TSSo
× 100
RESULTS &DISCUSSION
The characteristic of the industrial petrochemical wastewater
Parameter Units Petrochemical wastewater
effluent
Standard
A B
pH
pH 8.73 6.0 – 9.0 5.5 – 9.0
Chemical Oxygen Demand
mg/L 576 < 50 < 100
Suspended Solid
mg/L
0.011
< 50 < 100
Table 4.1
The characteristic of the industrial petrochemical wastewater
The percentage removal of COD and Suspended Solids for Fenton reagent on the
effect of dosages and for aluminium ion reagent on the effect of dosages.
Number (g) (mL) % Removal
Al3+ H2O2 pH COD TSS
1 0.5 1.4 7.12 - 55
2 0.5 1.6 7.08 - 55
3 0.5 1.8 7.06 - 18
1 0.5 1.65 4.46 - 82
2 0.7 1.65 4.46 - 64
3 1.1 1.65 3.87 - 45
4 1.3 1.65 3.77 - 65
Number (g) (mL) % Removal
Fe2+ H2O2 pH COD TSS
1 0.5 1.4 7.44 50 73
2 0.5 1.6 7.39 66 77
3 0.5 1.8 7.30 68 82
4 0.5 1.65 6.46 28 80
5 0.7 1.65 6.82 32 81
6 1.1 1.65 2.74 59 79
7 1.3 1.65 2.51 70 88
Fenton reagent on the effect of dosages Aluminium ion reagent on the effect of dosages
The experimental results are reported results of the research were shown in
Tables by using Fenton reagent, the range of percentages of removal of in the
effect of dosages in Fenton reagent was 68% and 70%,for COD and 82% and
88%,for TSS are respectively.
While the percentage removal in the effect of dosages by using Al3+ with different
dosage of H2O2 there was not the removal for COD as shown in the table .
However, the highest percentage of COD and TSS removal was 0 and 55%
respectively.
Effect of the amount of H2O2 for COD and TSS removal
47
64
67
0
10
20
30
40
50
60
70
80
1.4 1.6 1.8
%RemovalCOD
H2O2 Dosages mL
73
77
82
68
70
72
74
76
78
80
82
84
1.4 1.6 1.8
%RemovalTSS
H2O2 Dosages mL
Effect of the amount of Fe2+ for COD and TSS
removal.
16
18
38
47
0
5
10
15
20
25
30
35
40
45
50
0.5 0.7 1.1 1.3
%RemovalCOD
Fe2+ Dosages g
80
81
79
88
74
76
78
80
82
84
86
88
90
0.5 0.7 1.1 1.3
%RemovalTSS
Fe2+ Dosages g
PICTURES OF SAMPLES
Original sample of petrochemical wastewater. Petrochemical Wastewater before Treatment. Petrochemical Wastewater after Treatment.
Conclusion & Recommendation
Conclusion
• Petrochemical wastewater can be treated effectively by various chemical treatment processes. This study has shown
that the Fenton process is an efficient method of treating petrochemical wastewater.
• From the results obtained, we can see the trend of the results in removing all the parameters is in between 70% until
88 %. The best dosage of Fenton reagent is when H2O2 = 1.65ml and Fe2+ = 1.3g and also found, this treatment.
• In overall, feasibility or effectiveness of this treatment was controlled by the activity of hydroxyl free radicals ions
(very strong oxidation agent) produce. Increasing the number of free radicals ions produce, increasing the ability of
Fenton reagent treatment to destroy large molecules of pollutants in the wastewater.
Recommendation
• I. This treatment can be used for treat another type of wastewater.
• II. Other parameters can be tested in the study the feasibility of this Fenton reagent.
• III. In order to achieve standard A and Standard B were outlined by the Department of Environment Malaysia (DOE),
another treatment must be done (chemical processes or other) after using this treatment.
References
References
• Al-Malack, M., 2013. Treatment of petroleum refinery wastewater using cross flow and immersed membrane processes. Desalination and Water
Treatment.
• ALVES, A., 2013. Study of the Bioaugmentation of Grease Separators Using the GOR BioSystemTM.
• Augusto, O. & Miyamoto, S., 2011. Oxygen radicals and related species. Principles of free radical biomedicine.
• Awaleh, M. & Soubaneh, Y., 2014. Waste water treatment in chemical industries: the concept and current technologies. Hydrology: Current Research.
• Barbusiński, K., 2005. The modified Fenton process for decolorization of dye wastewater. Polish Journal of Environmental Studies.
• Diya’uddeen, B., Daud, W. & Aziz, A., 2011. Treatment technologies for petroleum refinery effluents: a review. Process Safety and.
• Fabio, S. Di et al., 2013. Are centralized MBRs coping with the current transition of large petrochemical areas? A pilot study in Porto-Marghera
(Venice). Chemical engineering.
• Gandhi, G. et al., 2014. IVF Lite-A new strategy for managing poor ovarian responders. IVF lite.
• Glaze, W., Kang, J. & Chapin, D., 1987. The chemistry of water treatment processes involving ozone, hydrogen peroxide and ultraviolet radiation.
• Hassan, H. & Hameed, B., 2011. Fe–clay as effective heterogeneous Fenton catalyst for the decolorization of Reactive Blue 4. Chemical Engineering
Journal.
• Huang, D. et al., 1991. Optical coherence tomography. Science (New York,.
• Jagadevan, S., Dobson, P. & Thompson, I., 2011. Harmonisation of chemical and biological process in development of a hybrid technology for
treatment of recalcitrant metalworking fluid. Bioresource technology.
• Karadag, D. et al., 2015. A review on anaerobic biofilm reactors for the treatment of dairy industry wastewater. Process Biochemistry.
• Karthikeyan, S. et al., 2011. Treatment of textile wastewater by homogeneous and heterogeneous Fenton oxidation processes. Desalination.
• Kato, H., Onda, Y. & Teramage, M., 2012. Depth distribution of 137 Cs, 134 Cs, and 131 I in soil profile after Fukushima Dai-ichi Nuclear Power
Plant accident. Journal of Environmental Radioactivity.
• Lou, J. & Huang, Y., 2009. Assessing the performance of wastewater treatment with the combination of Fenton and ferrite process. Environmental
monitoring and assessment.
• Lucas, M. & Peres, J., 2009. Removal of COD from olive mill wastewater by Fenton’s reagent: Kinetic study. Journal of hazardous materials.
• Ma, X. & Xia, H., 2009. Treatment of water-based printing ink wastewater by Fenton process combined with coagulation. Journal of hazardous
materials.
• Meriç, S., Kaptan, D. & Ölmez, T., 2004. Color and COD removal from wastewater containing Reactive Black 5 using Fenton’s oxidation process.
Chemosphere.
Activation of hydrogen peroxide by chemical reagent to reduce COD in petrochemical wastewater

Activation of hydrogen peroxide by chemical reagent to reduce COD in petrochemical wastewater

  • 1.
  • 2.
    Contents 1 • Introduction 2• Problem Statement 3 • Objective of the research 4 • Scope of the study 5 • Littre Review 6 • Methodology 7 • Result Analysis 8 • Conclusion & Recommendation 9 • References
  • 3.
  • 4.
    Introduction Nowadays modern societieshave been consistently exposed to environmental pollution (e.g. due to toxic compounds); due to by toxic compounds has been being gaining wider concern in modern developed society. Generally, petroleum refineries generate these polluted wastewater containing contain approximately 150-250 mg/L of Chemical Oxygen Demand (COD), 20-200 mg/L of phenol and 100-300 mg/L oil of (Al-Malack 2013). There are many ways that can be used several applications to remove COD. In the current work, however, this research will be focusing on using hydrogen peroxide to can reduce COD by direct oxidation (either complete or partial) of wastewater components. The performances of using use of iron-catalyzed H2O2 (i.e. Fenton's Reagent) and Al2(SO4)3 catalyzed H2O2 in reducing the amount of COD are compared.
  • 5.
  • 6.
    Typical petrochemical effluentshave significant concentrations of Elements such as suspended solids, organic matter, oil and grease, sulphide, ammonia, phenols, benzene, hydrocarbons, and COD can be found in a typical petrochemical effluent (e.g. wastewater), which would affect are very high which generated environmental pollutions by toxic compounds produced from them( Fabio, Malamis, Katsou, & Vecchiato, 2013). Industry wastewater is a serious problem as it is affecting the freshwater resources, human health, and agricultural productivity. The problem is more critical in the civilian and industrial areas where rapid water quality deterioration has caused widespread water-borne diseases and other recoverable damages to the environment. Wastewater treatment is very general and being applied throughout the world. Efforts of reducing COD must be developed in order to safeguard our environment. Here, this research Illustrates that reducing COD in petrochemical wastewater is an important process where the increase of COD causes pollution in environmental. Therefore, it is significant to reduce COD to keep a safe environment to beat this issue aqueous solutions of Fe(II)/H2O2 (also known as the Fenton’s reagent), because it is was found to be environmentally safe, cost effective and easy to operate. PROBLEMSTATEMENT
  • 7.
  • 8.
    Objective of theresearch The aim of this research is to reduce COD in the petrochemical wastewater by the activation of hydrogen peroxide using via two different reagents.
  • 9.
  • 10.
    Scope of thestudy 1. To determine the quality of petrochemical wastewater via parameters such as (COD, pH, and TSS) contributed to petrochemical wastewater pollution. 2. To study the effects of different activation reagents (i.e. Fe2+, Al3+) used to treat the wastewater. 3. To compare several parameters to COD removals such as the effects of concentration/dosage of H2O2, concentration, and dosages of Al2(SO4)3 and concentration and dosages of FeSO4 on the removal efficiency of COD. 4. To compare percentage reduction of COD using Fe2+ and Al3+ as activation reagent.
  • 11.
  • 12.
    Author Finding Awaleh &Soubaneh 2014 The resulting flock with the adsorbed oil is then separated, followed by sludge thickening and sludge dewatering Midhun et al. 2016 without coagulation/flocculation, sedimentation can remove only coarse suspended matter such as that observed this type of sedimentation typically takes place in a reservoir or sedimentation/clarification tank at the beginning of the treatment process Karadag et al. 2015 Adsorption occurs when the attractive forces at the carbon surface overcome the attractive forces of the liquid Glaze et al. 1987 Advanced Oxidation Processes (AOPs) are, in a broad sense, are a set of chemical treatment procedures adopted to remove organic (or inorganic) materials in wastewater via oxidation through reactions with hydroxyl radicals (·OH) . Mota et al. 2009 There are many methods that can be used to reduce the of pollutants from effluents Augusto & Miyamoto 2011 H2O2 is one of the most powerful oxidizers. Augusto & Miyamoto2011 . Fenton's chemistry uses hydrogen peroxides (H2O2) and iron salts where the effectiveness of H2O2 is improved by iron through the generation of highly reactive hydroxyl radicals Sax & DiMento 1974 Parameter Limit of Effluent Standard A and B
  • 13.
  • 14.
    Methodology In this study,in general, the equipment was used for experimental and analysis was (pH, digital reactor block (DRB200), DR 2800 portable spectrophotometer, the vacuum pump (300) and All-glass filtration assembly).
  • 15.
    PH meter The MettlerToledo pH meter was used to measure the pH value of the wastewater sample. Mettler Toledo pH meter
  • 16.
    Chemical Oxygen Demand(COD) Chemical Oxygen Demand (COD) was is analyzed by using the HACH Method. • The removal efficiency (% Removal) was calculated from the following formula: • • % Removal = Co _𝑐 𝑐o ×100 DR2800 Spectrophotometer.Digital Reactor Block (DRB200)
  • 17.
    Total suspended solids(TSS) vacuum pump (300) and All-glass filtration assembly. Suspended solid is analyzed by using gravimetric method (APHA, 1985). The TSS in the wastewater samples were calculated using the following formula equations g mL TSS = WB _WA Sample volume,mL × 100 The removal efficiency (% Removal) was calculated from the following formula: % Removal = TSSo _TSSt TSSo × 100
  • 18.
  • 19.
    The characteristic ofthe industrial petrochemical wastewater Parameter Units Petrochemical wastewater effluent Standard A B pH pH 8.73 6.0 – 9.0 5.5 – 9.0 Chemical Oxygen Demand mg/L 576 < 50 < 100 Suspended Solid mg/L 0.011 < 50 < 100 Table 4.1 The characteristic of the industrial petrochemical wastewater
  • 20.
    The percentage removalof COD and Suspended Solids for Fenton reagent on the effect of dosages and for aluminium ion reagent on the effect of dosages. Number (g) (mL) % Removal Al3+ H2O2 pH COD TSS 1 0.5 1.4 7.12 - 55 2 0.5 1.6 7.08 - 55 3 0.5 1.8 7.06 - 18 1 0.5 1.65 4.46 - 82 2 0.7 1.65 4.46 - 64 3 1.1 1.65 3.87 - 45 4 1.3 1.65 3.77 - 65 Number (g) (mL) % Removal Fe2+ H2O2 pH COD TSS 1 0.5 1.4 7.44 50 73 2 0.5 1.6 7.39 66 77 3 0.5 1.8 7.30 68 82 4 0.5 1.65 6.46 28 80 5 0.7 1.65 6.82 32 81 6 1.1 1.65 2.74 59 79 7 1.3 1.65 2.51 70 88 Fenton reagent on the effect of dosages Aluminium ion reagent on the effect of dosages The experimental results are reported results of the research were shown in Tables by using Fenton reagent, the range of percentages of removal of in the effect of dosages in Fenton reagent was 68% and 70%,for COD and 82% and 88%,for TSS are respectively. While the percentage removal in the effect of dosages by using Al3+ with different dosage of H2O2 there was not the removal for COD as shown in the table . However, the highest percentage of COD and TSS removal was 0 and 55% respectively.
  • 21.
    Effect of theamount of H2O2 for COD and TSS removal 47 64 67 0 10 20 30 40 50 60 70 80 1.4 1.6 1.8 %RemovalCOD H2O2 Dosages mL 73 77 82 68 70 72 74 76 78 80 82 84 1.4 1.6 1.8 %RemovalTSS H2O2 Dosages mL
  • 22.
    Effect of theamount of Fe2+ for COD and TSS removal. 16 18 38 47 0 5 10 15 20 25 30 35 40 45 50 0.5 0.7 1.1 1.3 %RemovalCOD Fe2+ Dosages g 80 81 79 88 74 76 78 80 82 84 86 88 90 0.5 0.7 1.1 1.3 %RemovalTSS Fe2+ Dosages g
  • 23.
    PICTURES OF SAMPLES Originalsample of petrochemical wastewater. Petrochemical Wastewater before Treatment. Petrochemical Wastewater after Treatment.
  • 24.
  • 25.
    Conclusion • Petrochemical wastewatercan be treated effectively by various chemical treatment processes. This study has shown that the Fenton process is an efficient method of treating petrochemical wastewater. • From the results obtained, we can see the trend of the results in removing all the parameters is in between 70% until 88 %. The best dosage of Fenton reagent is when H2O2 = 1.65ml and Fe2+ = 1.3g and also found, this treatment. • In overall, feasibility or effectiveness of this treatment was controlled by the activity of hydroxyl free radicals ions (very strong oxidation agent) produce. Increasing the number of free radicals ions produce, increasing the ability of Fenton reagent treatment to destroy large molecules of pollutants in the wastewater.
  • 26.
    Recommendation • I. Thistreatment can be used for treat another type of wastewater. • II. Other parameters can be tested in the study the feasibility of this Fenton reagent. • III. In order to achieve standard A and Standard B were outlined by the Department of Environment Malaysia (DOE), another treatment must be done (chemical processes or other) after using this treatment.
  • 27.
  • 28.
    References • Al-Malack, M.,2013. Treatment of petroleum refinery wastewater using cross flow and immersed membrane processes. Desalination and Water Treatment. • ALVES, A., 2013. Study of the Bioaugmentation of Grease Separators Using the GOR BioSystemTM. • Augusto, O. & Miyamoto, S., 2011. Oxygen radicals and related species. Principles of free radical biomedicine. • Awaleh, M. & Soubaneh, Y., 2014. Waste water treatment in chemical industries: the concept and current technologies. Hydrology: Current Research. • Barbusiński, K., 2005. The modified Fenton process for decolorization of dye wastewater. Polish Journal of Environmental Studies. • Diya’uddeen, B., Daud, W. & Aziz, A., 2011. Treatment technologies for petroleum refinery effluents: a review. Process Safety and. • Fabio, S. Di et al., 2013. Are centralized MBRs coping with the current transition of large petrochemical areas? A pilot study in Porto-Marghera (Venice). Chemical engineering. • Gandhi, G. et al., 2014. IVF Lite-A new strategy for managing poor ovarian responders. IVF lite. • Glaze, W., Kang, J. & Chapin, D., 1987. The chemistry of water treatment processes involving ozone, hydrogen peroxide and ultraviolet radiation. • Hassan, H. & Hameed, B., 2011. Fe–clay as effective heterogeneous Fenton catalyst for the decolorization of Reactive Blue 4. Chemical Engineering Journal. • Huang, D. et al., 1991. Optical coherence tomography. Science (New York,.
  • 29.
    • Jagadevan, S.,Dobson, P. & Thompson, I., 2011. Harmonisation of chemical and biological process in development of a hybrid technology for treatment of recalcitrant metalworking fluid. Bioresource technology. • Karadag, D. et al., 2015. A review on anaerobic biofilm reactors for the treatment of dairy industry wastewater. Process Biochemistry. • Karthikeyan, S. et al., 2011. Treatment of textile wastewater by homogeneous and heterogeneous Fenton oxidation processes. Desalination. • Kato, H., Onda, Y. & Teramage, M., 2012. Depth distribution of 137 Cs, 134 Cs, and 131 I in soil profile after Fukushima Dai-ichi Nuclear Power Plant accident. Journal of Environmental Radioactivity. • Lou, J. & Huang, Y., 2009. Assessing the performance of wastewater treatment with the combination of Fenton and ferrite process. Environmental monitoring and assessment. • Lucas, M. & Peres, J., 2009. Removal of COD from olive mill wastewater by Fenton’s reagent: Kinetic study. Journal of hazardous materials. • Ma, X. & Xia, H., 2009. Treatment of water-based printing ink wastewater by Fenton process combined with coagulation. Journal of hazardous materials. • Meriç, S., Kaptan, D. & Ölmez, T., 2004. Color and COD removal from wastewater containing Reactive Black 5 using Fenton’s oxidation process. Chemosphere.