The study aimed at color removal and COD degradation of
synthetic wastewater of methylene blue dye via photocatalysis using various spinel catalysts
prepared by different methods. The methylene blue dye with strong azo bond with structure
made up of autochrome and chromophore. The Azo dyes are widely used in textile, paper and
leather industries. The present study is essentially related to the degradation of selected
methylene blue and dye from synthetic dye wastewater however it has been extended to actual
industrial effluents. In order to control wastewater pollution due to dyes the UV-Photocatalytic
degradation technology has been carried out by some researchers using spinel catalysts. Spinel
catalysts are oxides with general formula AB2O4 where A and B are the rare earth, A has
octahedral site and B has tetrahedral site. alkaline earth, alkali metals and transition metal
cations which are expected to be able to overcome the limitations of semiconductors as
photocatalysts.
Photocatalysis has now become an emerging scientific discipline due to its interdisciplinary nature. The wide range of research groups is now working on different aspects of photocatalysis worldwide. It is one of the technology the world looking forward to address environmental as well as energy related issues. Hence we can call it as a technology for the future or a dream technology! We need to overcome too many hurdles to implement this technology in real life. Like any other discipline there is a lot of misunderstanding/ misconceptions in photocatalysis.
Most frequently cited article in the field of photocatalysis is by Fujishima and Honda published in 1972 in nature and it has been cited by the photocatalytic community as an origin of photocatalysis. This aspect is not true at all. This article cannot be the origin of photocatalysis. This article only promoted photocatalytic studies. The author itself, actually, started a research career in the “boom” of photocatalytic studies initiated by this article.
This small presentation aims to deliver some misconceptions like above in photocatalysis. The entire presentation is based on different personal commentaries written by Jean Mary Hermann and Bunsho Ohtani. Some recent articles relevant to the topic are collected by the speaker itself and put it in one platform.
degradation of pollution and photocatalysisPraveen Vaidya
The presentation deals with the use of conduction of photocatalytic reaction using the transition metal doped transparent semiconducting thinfilms. The precursor to film is prepared by the SILAR method, which is a chemical method.
Photocatalysis has now become an emerging scientific discipline due to its interdisciplinary nature. The wide range of research groups is now working on different aspects of photocatalysis worldwide. It is one of the technology the world looking forward to address environmental as well as energy related issues. Hence we can call it as a technology for the future or a dream technology! We need to overcome too many hurdles to implement this technology in real life. Like any other discipline there is a lot of misunderstanding/ misconceptions in photocatalysis.
Most frequently cited article in the field of photocatalysis is by Fujishima and Honda published in 1972 in nature and it has been cited by the photocatalytic community as an origin of photocatalysis. This aspect is not true at all. This article cannot be the origin of photocatalysis. This article only promoted photocatalytic studies. The author itself, actually, started a research career in the “boom” of photocatalytic studies initiated by this article.
This small presentation aims to deliver some misconceptions like above in photocatalysis. The entire presentation is based on different personal commentaries written by Jean Mary Hermann and Bunsho Ohtani. Some recent articles relevant to the topic are collected by the speaker itself and put it in one platform.
degradation of pollution and photocatalysisPraveen Vaidya
The presentation deals with the use of conduction of photocatalytic reaction using the transition metal doped transparent semiconducting thinfilms. The precursor to film is prepared by the SILAR method, which is a chemical method.
This presentation is about phtoocatalytic process and nanomaterials as photocatalyst. This is useful in the treatment of wastewater and environmental remediation applications.
Photocatalytic degradation of some organic dyes under solar light irradiation...Iranian Chemical Society
Nanoparticles of the ZnO and TiO2 were synthesized and the physicochemical properties of the compounds were characterized by IR, X-ray diffraction (XRD), scanning electron microscopy (SEM) and transmission electron microscopy (TEM). The XRD patterns of the ZnO and TiO2 nanoparticles could be indexed to hexagonal and rutile phase, respectively. Aggregated nanoparticles of ZnO and TiO2 with spherical-like shapes were observed with particle diameter in the range of 80-100 nm. These nanoparticles were used for photocatalytic degradation of various dyes, Rhodamine B (RhB), Methylene blue (MB) and Acridine orange (AO) under solar light irradiation at room temperature. Effect of the amount of catalyst on the rate of photodegradation was investigated. In general, because ZnO is unstable, due to incongruous dissolution to yield Zn(OH)2 on the ZnO particle surfaces and thus leading to catalyst inactivation,the catalytic activity of the system for photodegradation of dyes decreased dramatically when TiO2 was replaced by ZnO.
Structural and optical properties of molybdenum doped BiVO4 powders-Cce 2014MERUPO Victor
Molybdenum-doped BiVO4 powders were prepared by Sol-gel method. Monoclinic scheelite phase was confirmed by X-ray diffraction (XRD) patterns and micro-Raman vibrational bands. Substitution of molybdenum in crystal sites of BiVO4 was evidenced from XRD by higher angle 2θ shift of the characteristic peak (-121) and from Raman showing lower frequency shift of dominant peak from 831 to 822 cm-1 which corresponds to V-O symmetric stretching mode. The morphological properties were analyzed by FE-SEM which confirmed the formation of homogeneous spherical shaped particles with size around 200-300nm. Optical properties were analyzed by Diffuse Reflectance Spectra which show higher absorption in the range of 550-850nm. Optical band gap energies were calculated by using Kubelka-Munk formula, i.e, 2.46 eV for 2 wt% Mo-BiVO4 and 2.47eV for undoped BiVO4. This confirms that Mo-BiVO4 particles have the same band gap but induce higher absorption in the visible light region compared to BiVO4
The threat of global warming is high due to the extensive use of fossil fuels.Using non-renewable resources is a viable solution. Sunlight can be converted in two ways - into electrical energy and into chemical energy. Water splitting and CO2 are two important methods which can be used in solar cells.
metal organic framework-carbon capture and sequestrationVasiUddin Siddiqui
MOF is a porous crystal like a spunge having an enormous surface area and provide much more rooms for storage the gases preferentially hydrogen and carbon dioxide and work as storage for next generation fuel.
Solar Photocatalysis a green and novel technology for wastewater treatment. It is a sustainable way to harvest solar energy for treatment of wastewater at a lower cost thus helping in achieving some of the Sustainable Development Goals(i.e. Good Health and Wellbeing).
This is based on the advanced oxidation process i.e. generation of reactive oxygen species which can help in the degradation of pollutants
Photocatalytic application of TiO2/SiO2-based magnetic nanocomposite (Fe3O4@S...Iranian Chemical Society
In this research we have developed a treatment method for textile wastewater by TiO2/SiO2-based magnetic nanocomposite. Textile wastewater includes a large variety of dyes and chemicals and needs treatments. This manuscript presents a facile method for removing dyes from the textile wastewater by using TiO2/SiO2-based nanocomposite (Fe3O4@SiO2/TiO2) under UV irradiation. This magnetic nanocomposite, as photocatalytically active composite, is synthesized via solution method in mild conditions. A large range of cationic, anionic and neutral dyes including: methyl orange, methylene blue, neutral red, bromocresol green and methyl red are used for treatment investigations. Neutral red and bromocresol green have good results in reusing treatment. The high surface area of nanocomposites improve the kinetic of wastewater treatment. In this method, by using the magnetic properties of Fe3O4 nanoparticles, TiO2-based photocatalyst could be separated and reused for 3 times. The efficiency of this method is respectively 100% and 65% for low concentration (10 ppm) and high concentration (50 ppm) of neutral red and bromocrosol green after 3 h treatment. The efficiency of treatment using the second used nanocomposite was 90% for 10 ppm of the same dyes.
Decolourisation of Nigrosine WS dye by Solar Photo-fentonAkash Tikhe
My master's dissertation thesis topic- Decolorization of Nigrosine WS dye by Homogeneous Solar Photo-Fenton Method along with Intro, Method, Result, conclusion and suggestions.
This presentation is about phtoocatalytic process and nanomaterials as photocatalyst. This is useful in the treatment of wastewater and environmental remediation applications.
Photocatalytic degradation of some organic dyes under solar light irradiation...Iranian Chemical Society
Nanoparticles of the ZnO and TiO2 were synthesized and the physicochemical properties of the compounds were characterized by IR, X-ray diffraction (XRD), scanning electron microscopy (SEM) and transmission electron microscopy (TEM). The XRD patterns of the ZnO and TiO2 nanoparticles could be indexed to hexagonal and rutile phase, respectively. Aggregated nanoparticles of ZnO and TiO2 with spherical-like shapes were observed with particle diameter in the range of 80-100 nm. These nanoparticles were used for photocatalytic degradation of various dyes, Rhodamine B (RhB), Methylene blue (MB) and Acridine orange (AO) under solar light irradiation at room temperature. Effect of the amount of catalyst on the rate of photodegradation was investigated. In general, because ZnO is unstable, due to incongruous dissolution to yield Zn(OH)2 on the ZnO particle surfaces and thus leading to catalyst inactivation,the catalytic activity of the system for photodegradation of dyes decreased dramatically when TiO2 was replaced by ZnO.
Structural and optical properties of molybdenum doped BiVO4 powders-Cce 2014MERUPO Victor
Molybdenum-doped BiVO4 powders were prepared by Sol-gel method. Monoclinic scheelite phase was confirmed by X-ray diffraction (XRD) patterns and micro-Raman vibrational bands. Substitution of molybdenum in crystal sites of BiVO4 was evidenced from XRD by higher angle 2θ shift of the characteristic peak (-121) and from Raman showing lower frequency shift of dominant peak from 831 to 822 cm-1 which corresponds to V-O symmetric stretching mode. The morphological properties were analyzed by FE-SEM which confirmed the formation of homogeneous spherical shaped particles with size around 200-300nm. Optical properties were analyzed by Diffuse Reflectance Spectra which show higher absorption in the range of 550-850nm. Optical band gap energies were calculated by using Kubelka-Munk formula, i.e, 2.46 eV for 2 wt% Mo-BiVO4 and 2.47eV for undoped BiVO4. This confirms that Mo-BiVO4 particles have the same band gap but induce higher absorption in the visible light region compared to BiVO4
The threat of global warming is high due to the extensive use of fossil fuels.Using non-renewable resources is a viable solution. Sunlight can be converted in two ways - into electrical energy and into chemical energy. Water splitting and CO2 are two important methods which can be used in solar cells.
metal organic framework-carbon capture and sequestrationVasiUddin Siddiqui
MOF is a porous crystal like a spunge having an enormous surface area and provide much more rooms for storage the gases preferentially hydrogen and carbon dioxide and work as storage for next generation fuel.
Solar Photocatalysis a green and novel technology for wastewater treatment. It is a sustainable way to harvest solar energy for treatment of wastewater at a lower cost thus helping in achieving some of the Sustainable Development Goals(i.e. Good Health and Wellbeing).
This is based on the advanced oxidation process i.e. generation of reactive oxygen species which can help in the degradation of pollutants
Photocatalytic application of TiO2/SiO2-based magnetic nanocomposite (Fe3O4@S...Iranian Chemical Society
In this research we have developed a treatment method for textile wastewater by TiO2/SiO2-based magnetic nanocomposite. Textile wastewater includes a large variety of dyes and chemicals and needs treatments. This manuscript presents a facile method for removing dyes from the textile wastewater by using TiO2/SiO2-based nanocomposite (Fe3O4@SiO2/TiO2) under UV irradiation. This magnetic nanocomposite, as photocatalytically active composite, is synthesized via solution method in mild conditions. A large range of cationic, anionic and neutral dyes including: methyl orange, methylene blue, neutral red, bromocresol green and methyl red are used for treatment investigations. Neutral red and bromocresol green have good results in reusing treatment. The high surface area of nanocomposites improve the kinetic of wastewater treatment. In this method, by using the magnetic properties of Fe3O4 nanoparticles, TiO2-based photocatalyst could be separated and reused for 3 times. The efficiency of this method is respectively 100% and 65% for low concentration (10 ppm) and high concentration (50 ppm) of neutral red and bromocrosol green after 3 h treatment. The efficiency of treatment using the second used nanocomposite was 90% for 10 ppm of the same dyes.
Decolourisation of Nigrosine WS dye by Solar Photo-fentonAkash Tikhe
My master's dissertation thesis topic- Decolorization of Nigrosine WS dye by Homogeneous Solar Photo-Fenton Method along with Intro, Method, Result, conclusion and suggestions.
Visible Light Assisted Degradation of Eosin Yellow using Heteroatom Functiona...IJERA Editor
10 ppm EY dye were successfully photodegraded using visible light active 0.75wt% Ba & 0.25wt% Zr codoped
TiO2 nanomaterial that were synthesized by Sol-gel method as nanomaterials under irradiation for 20
minutes and characterized by various advanced instrumental techniques. The X-ray Diffraction Spectroscopic
showed that the prepared nanomaterial were in the anatase phase with 2θ at 25.3º. UV-visible Diffuse
Reflectance Spectra analysis explained that the dopants found in the TiO2, imparts a significance absorption
shift towards visible region and their exisistance were confirmed by X-ray Photoelectron Spectral data.
Quantitatively the formation of hydroxyl radical by the nanomaterial in aqueous solution under visible
light irradiation was investigated by the photoluminiscent technique. Finally the effects of different parameters
in the photocatalytic degradation of EY were established in aqueous solution
Electro-oxidation And Its Feasibility In Wastewater TreatmentSakib Shahriar
Electro-oxidation (EO) is one of the advanced oxidation processes (AOP) used in wastewater treatment. It is also called anodic oxidation. In this presentation, we can learn about the working principle, industrial applications, types of electrodes, and catalysts in the EO process. The advantages and disadvantages are described later. The main advantages of electro-oxidation are the formation of low sludge and large percentages of organic matter degradation. But the main drawbacks occur due to the requirement of large space and expense. EO is used in many types of wastewater treatment. Degradation of methyl orange azo dye in a recirculation flow plant system, treatment of wastewater containing aromatic amines, endocrine disruptors treatment, domestic water, industrial wastewater, synthetic dye effluent, olive mill wastewater, pulp mill wastewater, citric acid wastewater.
Sunlight induced removal of Rhodamine B from water through Semiconductor Pho...Hariprasad Narayanan
Application of Advanced Oxidation Processes (AOP) for the removal of toxic pollutants from water has been receiving increasing
attention in recent times. Photocatalysis using semiconductor oxides is one such AOP which is being investigated extensively for
the degradation of dyes in effluent water. This paper reports our findings on the sunlight induced photocatalytic removal of the
hazardous xanthene dye Rhodamine B from water, mediated by TiO2 and ‘platinum deposited TiO2’ (Pt/TiO2).Unlike in the case of
photocatalytic degradation of many organic pollutants which are driven by UV light, Rhodamine B can be removed in presence of
TiO2 even by visible light. Pt/TiO2 is ~5 times more active than TiO2 alone for the solar photocatalytic degradation of the dye,
which is attributed to extension of the absorption of light to the visible range and retardation of the recombination of
photogenerated electrons and holes. The dye itself can absorb visible light and act as a photo sensitizer to activate TiO2. The
effects of various parameters such as catalyst loading, concentration of the dye, pH, Pt concentration in Pt/TiO2, externallyadded
H2O2 etc on the adsorption and /or degradation of the dye are evaluated. The degradation of the dye proceeds through
intermediates and complete removal of Total Organic Carbon (TOC) is achieved many hours after the decolorisation of the dye.
The rate of degradation decreases beyond a critical concentration of the dye, possibly due to reduction in the path length of
photons in deeply colored solution. The higher degradation in alkaline pH is explained in terms of the ionization state of the
catalyst surface and the enhanced adsorption facilitated by the electrostatic attraction between the negatively charged catalyst
surface and the zwitter ionic form of the dye. H2O2, upto a critical concentration, accelerates the degradation. The observations are
critically analysed and suitable mechanism for the photocatalytic mineralisation of RhB is proposed.
Degradation of Paracetamol by Electro-Fenton and Photoelectro-Fenton Processe...Oswar Mungkasa
prepared by M.C. Lu *, M.L.Veciana**, M.D.G. de Luna*** * Department of Environmental Resources Management, Chia Nan University of Pharmacy and Science, Tainan 717, Taiwan **Environmental Engineering Graduate Program, University of the Philippines, 1011 Diliman, Quezon City, Philippines *** Department of Chemical Engineering, University of the Philippines, 1011 Diliman, Quezon City, Phi for Urban Environments in Asia, 25-28 May 2011, Manila, Philippines. organized by International Water Association (IWA).
Hierarchical Digital Twin of a Naval Power SystemKerry Sado
A hierarchical digital twin of a Naval DC power system has been developed and experimentally verified. Similar to other state-of-the-art digital twins, this technology creates a digital replica of the physical system executed in real-time or faster, which can modify hardware controls. However, its advantage stems from distributing computational efforts by utilizing a hierarchical structure composed of lower-level digital twin blocks and a higher-level system digital twin. Each digital twin block is associated with a physical subsystem of the hardware and communicates with a singular system digital twin, which creates a system-level response. By extracting information from each level of the hierarchy, power system controls of the hardware were reconfigured autonomously. This hierarchical digital twin development offers several advantages over other digital twins, particularly in the field of naval power systems. The hierarchical structure allows for greater computational efficiency and scalability while the ability to autonomously reconfigure hardware controls offers increased flexibility and responsiveness. The hierarchical decomposition and models utilized were well aligned with the physical twin, as indicated by the maximum deviations between the developed digital twin hierarchy and the hardware.
Welcome to WIPAC Monthly the magazine brought to you by the LinkedIn Group Water Industry Process Automation & Control.
In this month's edition, along with this month's industry news to celebrate the 13 years since the group was created we have articles including
A case study of the used of Advanced Process Control at the Wastewater Treatment works at Lleida in Spain
A look back on an article on smart wastewater networks in order to see how the industry has measured up in the interim around the adoption of Digital Transformation in the Water Industry.
Industrial Training at Shahjalal Fertilizer Company Limited (SFCL)MdTanvirMahtab2
This presentation is about the working procedure of Shahjalal Fertilizer Company Limited (SFCL). A Govt. owned Company of Bangladesh Chemical Industries Corporation under Ministry of Industries.
Overview of the fundamental roles in Hydropower generation and the components involved in wider Electrical Engineering.
This paper presents the design and construction of hydroelectric dams from the hydrologist’s survey of the valley before construction, all aspects and involved disciplines, fluid dynamics, structural engineering, generation and mains frequency regulation to the very transmission of power through the network in the United Kingdom.
Author: Robbie Edward Sayers
Collaborators and co editors: Charlie Sims and Connor Healey.
(C) 2024 Robbie E. Sayers
Cosmetic shop management system project report.pdfKamal Acharya
Buying new cosmetic products is difficult. It can even be scary for those who have sensitive skin and are prone to skin trouble. The information needed to alleviate this problem is on the back of each product, but it's thought to interpret those ingredient lists unless you have a background in chemistry.
Instead of buying and hoping for the best, we can use data science to help us predict which products may be good fits for us. It includes various function programs to do the above mentioned tasks.
Data file handling has been effectively used in the program.
The automated cosmetic shop management system should deal with the automation of general workflow and administration process of the shop. The main processes of the system focus on customer's request where the system is able to search the most appropriate products and deliver it to the customers. It should help the employees to quickly identify the list of cosmetic product that have reached the minimum quantity and also keep a track of expired date for each cosmetic product. It should help the employees to find the rack number in which the product is placed.It is also Faster and more efficient way.
Explore the innovative world of trenchless pipe repair with our comprehensive guide, "The Benefits and Techniques of Trenchless Pipe Repair." This document delves into the modern methods of repairing underground pipes without the need for extensive excavation, highlighting the numerous advantages and the latest techniques used in the industry.
Learn about the cost savings, reduced environmental impact, and minimal disruption associated with trenchless technology. Discover detailed explanations of popular techniques such as pipe bursting, cured-in-place pipe (CIPP) lining, and directional drilling. Understand how these methods can be applied to various types of infrastructure, from residential plumbing to large-scale municipal systems.
Ideal for homeowners, contractors, engineers, and anyone interested in modern plumbing solutions, this guide provides valuable insights into why trenchless pipe repair is becoming the preferred choice for pipe rehabilitation. Stay informed about the latest advancements and best practices in the field.
Synthesis of Spinel based Catalysts by Wet chemical methods for Colour Removal from Dyes Waste water
1. Project on
Synthesis of Spinel based Catalysts by Wet
chemical methods for Colour Removal from
Dyes Waste water
Presented By
Gandhi Yash (160170105017) Meda Sanjay (160170105027)
Patel Parth (160170105040) Rana Pranav(160170105046)
Guide by :
Dr. Femina Patel
CHEMICAL ENGINEERING DEPARTMENT
Year 2019-20 1
2. Contents
Industrial Effluents
Limits of Discharge of effluents from Industry
Current Treatments
Objectives
Literature Survey
•Materials and experiment methods
Summary and Conclusions
References
2
3. Industrial effluents
• Water resources contaminated by various industrial
activities
• Responsible industries are textile, paper, plastic, cosmetic,
dye and pigments etc. (30 to 40 % dyes remains in effluent
with toxic compound)
• Industrial effluent rich in COD, BOD, TOC, dyes etc.
• Serious environmental and health problems generated
• Conventional techniques use to eliminate dyes are difficult
• In India the Water (Prevention and Control of Pollution) Act
was enhanced in the year 15 Oct 1974 to control and
prevent water pollution
• 11 CETPs near Ahmadabad and 33 in all over Gujarat
• Treatments has operational limitations
3
4. Limits of Discharge of effluent from Industry
4
Dye
Organic compound
AuxochromsChromophore
-N=N-
=C=O
=C=C=
-NO2
-NH3
-COOH
-OH
-SO3H
Parameters Discharge limit
pH 6.5-8.5
Temperature 45 ˚C
100 (Pt-Co)/Hazen
COD 250 (mg/L)
BOD 100 (mg/L)
Oil, Grease 10 (mg/L)
Fluoride 1.5 (mg/L)
Sulfide 2.0 (mg/L)
Cyanide 0.2 (mg/L)
TDS 5000 (mg/L)
Sulfates 1000 (mg/L)
Chlorides 600 (mg/L)
Colour
5. Man-made Colorants
• Textiles
• Rubber
• Plastic
• Leather
• Cosmetics
• Paper
• Photographic
Natural Colorants
• Aquatic plants etc.
5
Dyes are:
• Complex aromatic structure
• Very stable
• Difficult to biodegrade
Sources of the dyes
7. Different Processes Used in Industry for dye degradation
Treatment methods Advantages Disadvantages
Physical Method
Membrane Separation Can decolorize all types of chemicals class dye Sludge generation, Expensive, High Pressure
Ion Exchange Operative with no loss of regeneration Not effective for dispense dyes
Adsorption Effective, high capacity
Regeneration expensive, ineffective against vat
and dispense dye
Electrolysis Varying degree of success in colour removal By product, not applied for full scale
Chemical Method
Oxidation Rapid and Proficient process High energy cost
Coagulation Simple, Economically feasible Sludge production
Biological Method
Aerobic
Rapid and efficient process, efficient breakdown of organic
pollutants
Large amount of electrical energy, excess sludge
production
Anaerobic More environmentally friendly Less efficient than aerobic
8. Advance Oxidation Process (AOP)
• Utilize the hydroxyl radical (·OH) for oxidation
• Advantages: (1) Fast reaction rates
(2) Non selective oxidation
• Complete mineralization of pollutants
8
Advance
Oxidation
Process
Photocatalysis Fenton Based Ozone based Electrochemical
9. AOPs Advantages Disadvantages
Fenton’s Reaction
No potential formation of
bromate by product
Iron sludge generation due to
combined flocculation of the
reagent and the organic
compounds
Photocatalysis Performance under solar
irradiation
If the catalyst is added as a
slurry, separation step is
required
H2O2/UV
Full scale drinking water
treatment system exists
Potential bromate by product
Advantages and disadvantages of Advanced oxidation Processes (AOPs)
10. Mechanism of Photocatalyst
10
Odour
Virus
Stain
Surface of the photocatalyst
Organic
compound
Electrons(+ and - )
H2O (moisture)
+
- - - - - - - - - - - - -
O2 O2- Super oxide anion
H2O OH
+ + + + + + + + + + + +
Decomposition and detoxify
Finally H2O and CO2
OH, O2- organic compound
Light energy
Due to catalyst property decomposition
-
+
Advantages of photocatalysis
• Low energy consumption
• Complete mineralization of
pollutants into harmless
product
• Oxidation is at or above
ambient condition
Types of Photocatalyst
• Semi conductor
• Spinel
• perovskite
11. Semiconductor Band gap (eV) Spinel Band gap (eV)
TiO2 3.0-3.2 ZnRh2O4 1.2
Diamond 5.4 CaFe2O4 1.9
WO3 2.7 MgFe2O4 2.18
ZnO 3.2 ZnFe2O4 1.92
SnO2 3.5 NiFe2O4 2.19
SrTiO3 3.4 CuFe2O4 1.32
11
12. 12
Semiconductor
Mixed metal oxide Spinel AB2O4
TiO2 , ZnO , Fe2O3, Cds, SnO2, CeO2
Photocatalyst
• 4% of solar energy
• Wide band gap >3 eV
• Active only in UV range
• Less O-2 and OH⋅ radical
• High dosage
• Separation problem
• Sludge disposal
• Expensive process
• ZnO corrode in H2O < 7 pH
• Largest portion of solar spectrum utilised
• Narrow band gap (<3 eV)
• UV and visible range
• Radical formation is rapid (OH⋅ and O-2)
• Time & dosage minimum
• Batch, continuous process at room temp.
• Cost efficient
• Good electrical & magnetic properties
• Easily separated from water and reused
• Takes O2 from free atmosphere
• Finally CO2 and H2O realised
AII = divalent cation
Eg: Ni, Mg, Zn, Mn, Fe
BIII = trivalent cation
Eg: Al, Ga, Ti
NiFe2O4, CoFe2O4, Fe3O4, ZnFe2O4, MgFe2O4, FeCr2O4
13. Objectives
The main objective is to develop Spinel based Catalyst for
Photocatalytic degradation of Dye.
The specific objectives are as follows:
• To synthesis of Spinel Based Catalyst (NiFe2O4) by co-precipitation
and Citrate methods
• To study degradation of Reactive dye via Photo-catalysis by using
Spinel Based Catalyst
• Investigation of suitability of Spinel Based Catalyst in order to screen
suitable catalyst preparation method
• To study the effect of operating parameters such as pH, initial dye
concentration, Dosage of catalyst
• Detailed characterization of suitable catalyst
13
14. Literature survey
Sr.
No.
Spinel/Other
catalyst
Targeted
Pollutant
Method
Characterization
Techniques
Experimental
condition
Results Reference
1 TiO2
Acid orange (AO7),
λmax=484 nm
TiO2/UV LC/MS
Lamp= Artificial UV-Light (30 Watt)
pH=2-10
Dye-5-100ppm, Dosage=0.5-2g/L
COD=72.41% in 2.5 h and
decolorization 79.58%.
Longer irradiation time
required
Bansal et al.,
2010
2 ZnO
Methylene Blue ,
λmax 665 nm
ZnO/UV UV, BET, SEM, FTIR
UV Lamp=14 W
Dosage =0.4 g, Temperature = 30 ̊C
pH = 7.0,
initial dye concentration = 50 mg/l,
Colour Removal 58 %, COD
Removal =24% ,time 2 h
Chakrabati et
al., 2004
3 ZnO
Eosin Y. A, λmax
516 nm
ZnO/UV UV, BET, SEM, FTIR
UV Lamp=14 W
Dosage =0.4 g, Temperature = 30 ̊C
pH = 7.0
initial dye concentration = 50 mg/l
Colour Removal 39 %, COD
Removal =8.1% ,time 2 h
Chakrabati et
al., 2004
4
ZnFe2O4 Methyl Orange
λmax=400 nm.
CP XRD
UV lamp =230 V
Dosage=0.2 g into 50 ml. Dye,
Dark =30min.
75% of methyl orange
decomposes within 60 min
of irradiation
Jadhav et al.,
2011
5 ZnFe2O4
Acid Red 88,
λmax =505 nm.
SG
XRD, SEM,
HRTEM, BET, FTIR,
pH = 3.2–10.7,
Temp. = 20–60 ̊C,
Dye = 200 mL. (10-56 mg/L)
MB dye decreased to 96.8%
Konicki et al.,
2013
6
MnFe2O4 Methyl Orange,
λmax =507nm
SG
XRD, SEM, BET,
TPR, XPS
Dosage=0.1g
Dye = 200 ml (30 mg in L)
Stirring =30 min
MO degradation efficiency
up to 98%.
Zhang et al.,
2013
14
Note:
(SG-sol-gel, CP-co-precipitation)
15. Sr. No.
Spinel/Other
catalyst
Targeted
Pollutant
Method
Characterization
Techniques
Experimental
condition
Results Reference
7
CuFe2O4 Acid Red 206,
λmax=513 nm
SG XRD, FT-IR, UV
pH = 4, 10, 2,
Mercury lamps.
Speed = 250 rpm
3h color removal
Bagheri et
al., 2013
8
NiFe2O4
Di-n-butyl phthalate SG XRD, BET, FTIR, XPS
Lamp=1.0-L global glass reactor, 25 °C,
pH=7.7,
Dosage=0.01 g,
Use=40 mLmin-1 ozone flow rate,
0.45μm filter paper.
100% removal after 60
min
Ren et al.,
2012
9 NiFe2O4
Reactive Blue 5
λmax=599 nm
MW=774.16 g/mol,
SG XRD, DTA, FT-IR,
pH = 1,
Temp. = 25 °C,
Dosage=50 mgl−1,
Time =10 min.
90% adsorption efficient,
reusable adsorbent
Khorsavi et
al., 2013
10 NiFe2O4 Reactive Blue HT XRD, TEM, SEM
Lamp=300W UV-visible lamp, Distance
between the lamp and test solution was
about 10 cm,
Temp. = 25 ̊C,
Dosage =0.20 g,
Solution=50 mL test
Seven cyclic tests
stable, and easy to
separate using an
external magnet 98.7%
decolorization ratio
Liu et al.,
2012
11 NiFe2O4
Brilliant Green,
λmax=623nm,
TOC
CP, MW XRD, FTIR
Lamp=Microwave,
Dye = 50 mL,
Dosage = 0.8%
Dye removal 97%, TOC
91% time 2.0 min
Zhang et al.,
2011
12
TiO2-ZnFe2O4 Methyl Red,Thymol
Blue, λmax=425 nm
CT, AC, HT
XRD, BET, TEM, UV,
DR-UV, EDAX
Lamp= UV radiation 450 W Xe arc, 100
cm3 pyrex glass, Vessel and lamp 8 W,
wavelength 253, ± 50 nm,
Dye=50 cm3 of 50 ppm,
Dosage =100 mg
Degradation of 90, 75,
64 and 60% in the 1st,
2nd, 3rd and 4th cycles
Hankare et
al., 2011
15
Note:
(SG-sol-gel, CP-co-precipitation, HT-hydrothermal, MW-Microwave, AC-auto combustion, CT-citrate)
16. Sr. No.
Spinel/Other
catalyst
Targeted
Pollutant
Method
Characterization
Techniques
Experimental
condition
Results Reference
13
CoFe2O4
and CoFe2O4/TiO2
Reactive Red 120 ,
λmax = 512 nm
CP XRD, TEM, SEM, UV
Lamp=150W tungsten halogen
lamp
(400 nm intensity),
Temp.=ambient,
Stirred= 45 min,
pH =6.0,
Stirring = 45 min
Synergetic enhancement in
the photocatalytic
degradation.
Satishkumar
et al., 2013a
14 ZnFe2O4/SrFe12O19
Methylene Blue
(MB),
λmax=420 nm
CP
FTIR, XRD, SEM,
BET, XPS, VSM, UV–
vis.
Lamp=500 W Xe, visible,
pH=Neutral
Degradation rate was still
morethan 70% when the
composite was reused for
four times
Xie et al.,
2013
15
CoCr2O4
and CoCr2O4/TiO2
Methylene Blue
(MB), λmax= 664
nm
Methyl Orange,
λmax= 464 nm
SG
XRD, SEM, TEM,
UV- vis.
Lamp=400W halogen lamp,
Stirring = 50 min,
Dosage =20 mg,
pH= Neutral
Molar ratio=7:10
MB and MO dye decreased
up to 91% & 82%
Shojaei et al.,
2013
16
CoFe2O4
and CoFe2O4/ZnO
Direct Blue 71 (azo
dye), λmax= 594 nm
CP
XRD, SEM, TEM,
UV-vis, TOC
analyzer.
Lamp=150W halogen lamp .
Stirring = 45 min.
Dosage =1.6 g/L.
pH= Neutral.
71% of TOC was removed
within 5 hours with 3 times
recycle.
Satishkumar
et al., 2013
16
Note:
(SG-sol-gel, CP-co-precipitation)
17. Various Synthesis method of photocatalyst
SynthesisMethods
Wet Chemical
Co-Precipitation
Sol-gel
Citrate
Dry Chemical Ceramic
17
18. (A) Co-precipitation method (CP) (B) Citrate method (CT)
18
Preparation method of Photocatalyst by Co-precipitation & Citrate method
Nitrate salts solution
pH = 10
Filtration
1M Na2CO3
drop wise addition
Precipitate ageing
for 30 min
Calcination at
700 0
C for 5 h
Catalyst
Drying at 110 0
C
over night
Crushing
19. Preparation of NiFe2O4 by Co-precipitation method
19
Cake after filtration
Nickle Nitrate Ferric Nitrate solution of solution of
nickel nitrate ferric nitrate
Precipitation formation by adding
1M Na2CO3 (pH=10)
Washing & filtration
Drying at 110 ⁰C
for 16 h
Calcined at 750 ⁰C
for 5 h
NiFe2O4
mixing of above two
20. Preparation of NiFe2O4 by Co-precipitation method
20
Cake after filtration
Nickle Nitrate Ferric Nitrate solution of solution of
nickel nitrate ferric nitrate
Precipitation formation by adding
1M NaOH (pH=10)
Washing & filtration
Drying at 110 ⁰C
for 16 h
Calcined at 750 ⁰C
for 5 h
NiFe2O4
mixing of above two
21. Preparation of catalyst NiFe2O4 by Citrate method
21
Gel after Heating
Nickle Nitrate Ferric Nitrate solution of solution of
nickel nitrate ferric nitrate
Adding Citric acidHeating at 80 ⁰C till Gel Formation
Drying at 110 ⁰C
for 16 h
mixing of above two
Calcined at 750 ⁰C
for 5 h Final catalyst
22. Photocatalytic degradation of dye
22
150 ppm solution
of RB-21
pH of the dye solution 1 gm NiFe2O4 Catalyst
Stirring in dark for 30
min.
Stirring in sunlight
Sample collected by every 30 min.
23. List of Experiments
Sr No. Catalyst Synthesis method Dye
Amount of
Solution (ml)
Concentration of
dye (ppm)
pH of
solution
Dose of
catalyst (gm)
Result
1 NiFe2O4
Co-Precipitation
(Na2CO3)
Methylene Blue 50 150 7 0.5 No result found in terms of colour
2 NiFe2O4
Co-Precipitation
(Na2CO3)
Methylene Blue 100 100 7 1 Slight colour change within 18 hrs.
3 NiFe2O4 Citrate Methylene Blue 100 100 7 1 No result found in terms of colour
4 NiFe2O4 Citrate Methylene Blue 100 100 4 1 No result found in terms of colour
5 NiFe2O4 Citrate Methylene Blue 100 100 10 1 No result found in terms of colour
6 NiFe2O4
Co-Precipitation
(NaOH)
Methylene Blue 100 100 7 1 No result found in terms of colour
7 NiFe2O4
Co-Precipitation
(NaOH)
Methylene Blue 100 100 4 1 No result found in terms of colour
8 NiFe2O4
Co-Precipitation
(NaOH)
Methylene Blue 100 100 10 1 No result found in terms of colour
9 NiFe2O4
Co-Precipitation
(NaOH)
Methylene Blue 100 50 10 0.5 No result found in terms of colour
10 NiFe2O4
Co-Precipitation
(NaOH)
Methylene Blue 100 50 4 0.5 No result found in terms of colour
24. Sr No. Catalyst Synthesis method Dye
Amount of
Solution (ml)
Concentration of dye
(ppm)
pH of
solution
Dose of
catalyst (gm)
Result
11 NiFe2O4
Co-Precipitation
(NaOH)
Methylene Blue 100 50 7 0.5 No result found in terms of colour
12 NiFe2O4 Citrate Magenta HB 100 100 7 0.5 No result found in terms of colour
13 NiFe2O4 Citrate Magenta HB 100 100 7 1 No result found in terms of colour
14 NiFe2O4 Citrate Magenta HB 100 100 4 1 No result found in terms of colour
15 NiFe2O4 Citrate Magenta HB 100 100 10 1 No result found in terms of colour
16 NiFe2O4
Co-Precipitation
(Na2CO3)
Magenta HB 100 100 7 1 No result found in terms of colour
17 NiFe2O4
Co-Precipitation
(Na2O3)
Magenta HB 100 100 3 1 No result found in terms of colour
18 NiFe2O4
Co-Precipitation
(Na2CO3)
Magenta HB 100 100 10 1 No result found in terms of colour
20 NiFe2O4 Citrate Methyl Orange 100 50 7 0.5 No result found in terms of colour
21 NiFe2O4 Citrate Methyl Orange 100 50 3 0.5 No result found in terms of colour
22 NiFe2O4 Citrate Methyl Orange 100 50 10 0.5 No result found in terms of colour
25. Sr No. Catalyst Synthesis method Dye
Amount of
Solution (ml)
Concentration of dye
(ppm)
pH of
solution
Dose of
catalyst (gm)
Result
23 NiFe2O4
Co-Precipitation
(Na2CO3)
Methyl Orange 100 50 7 1 No result found in terms of colour
24 NiFe2O4 Citrate
Reactive Turquoise Blue
21
100 100 7 1 No result found in terms of colour
25 NiFe2O4 Citrate
Reactive Turquoise Blue
21
100 100 10 1 No result found in terms of colour
26 NiFe2O4 Citrate
Reactive Turquoise Blue
21
100 100 4 1 No result found in terms of colour
27 NiFe2O4
Co-Precipitation
(Na2CO3)
Reactive Turquoise Blue
21
100 100 7 1 Slight colour change within 24 hrs.
28 NiFe2O4
Co-Precipitation
(Na2CO3)
Reactive Turquoise Blue
21
100
50 + 1 ml Hydrogen
peroxide
7 1 Yes , colour removed within 150 mins
29 NiFe2O4
Co-Precipitation
(Na2CO3)
Reactive Turquoise Blue
21
100
100 + 1 ml Hydrogen
peroxide
7 1 Yes , colour removed within 180 mins
30 NiFe2O4
Co-Precipitation
(Na2CO3)
Reactive Turquoise Blue
21
100
150+ 1 ml Hydrogen
peroxide
7 1 Yes , colour removed within 240 mins
26. Summary and Conclusions
• The reactive turquoise blue (RB21) dye was treated for degradation of
industrial wastewater using spinel catalyst
• Among all spinel catalyst prepared NiFe2O4 and ZnFe2O4 gain promising
result with synthetic dye and industrial wastewater degradation.
• Photocatalytic activity were optimized as stirring the sample, requirement
of sample, initial concentration of dye, pH 7, catalyst dosage, irradiation
time
• From the experiment we conclude that using spinel based catalyst
(NiFe2O4) 75-80 % color Remove and also 70 % COD Reduction in 240
min for initial dye concentration of 50 mg/L in proper sunlight
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