Modification of coconut shell activated carbon with an azo ligand: 1, 2– dihydro-1, 5- dimethyl-2 phenyl-4- (e)–(2,3,4- trihydrophenyl)-3h-pyrazol-3-one (ddptp) and its potentials for the removal of cd2+, pb2+ and ni2+ from polluted water.

 

Table Of Contents


  • <p> Title – – – – – – – – – – i<br>Approval – – – – – – – – – – ii<br>Certification – – – – – – – – – íii<br>Declaration – – – – – – – – – iv<br>Dedication – – – – – – – – – – v<br>Acknowledgment – – – – – – – – – vi<br>Abstract – – – – – – – – – – vii<br>Table of contents – – – – – – – – – viii-xiv<br>List of abbreviations- – – – – – – – – – xv<br>List of table – – – – – – – – – – xvi-xvii<br>List of figures – – – – – – – – – – xviii-xx<br>List of symbols – – – – – – – – – xxi-xxii<br>List of Schemes – – – – – – – – – xxiii<br>

Chapter ONE

INTRODUCTION

  • <br>1.
  • 0.Introduction – – – – – – – – 1<br>
  • 1.1Background of the Study – – – – – – – 1<br>1.
  • 2.Statement of the Problem – – – – – – – 4<br>1.
  • 3.The Justification of the Research- – – – – – – 4<br>1.
  • 4.Aims and Objectives of the Research – – – – – 5<br>ix<br>

Chapter TWO

LITERATURE REVIEW

  • <br>
  • 2.0Literature Review – – – – – – – – .6<br>
  • 2.1Review of some work Related to this Research – – – – 6<br>
  • 2.2Heavy metals – – – – – – – – – 12<br>2.
  • 2.1Beneficial Heavy Metals – – – – – – – 12<br>2.
  • 2.2Toxic Heavy Metals – – – – – – – 13<br>2.
  • 2.3Cadmium – – – – – – – – 13<br>2.
  • 2.4Properties of cadmium – – – – – – 14<br>2.
  • 2.5Applications – – – – – – – – 14<br>2.
  • 2.6Health effects of Cadmium – – – – – – 15<br>2.
  • 2.7Lead – – – – – – – – – 15<br>2.
  • 2.8Properties of lead – – – – – – – 17<br>2.
  • 2.9Applications – – – – – – – – 17<br>2.
  • 2.10Health effects of lead – – – – – – – 18<br>2.
  • 2.11Nickel – – – – – – – – 19<br>2.
  • 2.12Properties of Nikel – – – – – – – 19<br>2.
  • 2.13Applications – – – – – – – 20<br>2.
  • 2.14Health effect of Nikel – – – – – – .20<br>
  • 2.3Pollution by Cd2+, Ni2+ and Pd2+ – – – – – – 22<br>2.
  • 3.1Cadmium in the environment – – – – – – 22<br>2.
  • 3.2Environmental effects of cadmium – – – – – – 23<br>x<br>2.
  • 3.3Lead in the environment – – – – – – 24<br>2.
  • 3.4Environmental effects of lead – – – – – – 24<br>2.
  • 3.5Nikel in the environment – – – – – – 25<br>2.
  • 3.6Effects of nickel on the environment – – – – – 25<br>2.
  • 3.7Atomic Absorption Spectroscopy (AAS) – – – – 26<br>
  • 2.4Adsorption Mechanism – – – – – – 29<br>2.
  • 4.1What is Adsorption? – – – – – – – 29<br>2.
  • 4.2How Adsorption occurs – – – – – – 29<br>2.
  • 4.3Adsorption occurs – – – – – – – 30<br>2.
  • 4.4Adsorption in solids – – – – – – – 30<br>2.
  • 4.5Facts about Adsorption Process – – – – – 31<br>2.
  • 4.6Type of Adsorption – – – – – – – 32<br>2.
  • 4.7Applications of Adsorption – – – – – – 35<br>2.
  • 4.8Factors on which Adsorption Depends – – – – 37<br>2.
  • 5.0Adsorption Isotherm – – – – – – – 38<br>2.
  • 5.1The Langmuir isotherm – – – – – – 38<br>2.
  • 5.2The Freundlick isotherm – – – – – – 39<br>
  • 2.6Displacement of Adsorbed Metals by Competitive Ions in Solution – – 41<br>
  • 2.7The Ligand; Azo Ligand – – – – – – 42<br>2.
  • 7.1Definition – – – – – – – – 42<br>2.
  • 7.2Diazotization – – – – – – – – 42<br>xi<br>2.
  • 7.3Azo Coupling – – – – – – – 43<br>2.
  • 7.44-Amionantipyrine – – – – – – – 43<br>2.
  • 7.5Properties of 4- Amionantipyrine – – – – – 43<br>2.
  • 7.6Pyrogallol – – – – – – – – 44<br>2.
  • 7.7Properties of pyrogallol – – – – – – 44<br>
  • 2.8Activated Carbon – – – – – – – 45<br>2.
  • 8.1Definition of activated Carbon – – – – – 45<br>2.
  • 8.2Historical Development of Activated Carbon- – – – 46<br>2.
  • 8.3Properties of Activated Charcoal – – – – – 47<br>2.
  • 8.4Chemical properties of Activated Carbon – – – – 52<br>2.
  • 8.5Classification – – – – – – – – 54<br>2.
  • 8.6Applications of Activated Charcoal – – – – – 57<br>2.
  • 8.7Factors in which Selection of Raw Material Depends on – – 61<br>2.
  • 8.8The Coconut Shell – – – – – – – 61<br>2.
  • 8.9Uses of Coconut Shell Activated Carbon and its Advantages<br>over other ACs – – – – – – – 64<br>2.
  • 8.10Activation of Coconut Shell Carbon – – – – – 64<br>

Chapter THREE

RESEARCH METHODOLOGY

  • <br>
  • 3.0Materials and Methods – – – – – – – 66<br>
  • 3.1Apparatus – – – – – – – – – 66<br>
  • 3.2Preparation of Reagents – – – – – – – 66<br>xii<br>3.
  • 2.1Reagents- – – – – – – – – – 66<br>3.
  • 2.2Preparation of
  • 0.5Moldm-3 of CH3COOH (Acetic Acid) – – – 67<br>3.
  • 2.3Preparation of
  • 0.5Moldm-3 of HNO3 – – – – – – 67<br>3.
  • 2.4Preparation of 1000 ppm Pb(NO3)2 solution – – – – – 67<br>3.
  • 2.5Preparation of 1000 ppm Cd(NO3)2 4H2O solution – – – – 67<br>3.
  • 2.6Preparation of 1000ppm NiCl2. 6H2O solution – – – – 68<br>3.
  • 3.Synthesis of the Ligand – – – – – – – 68<br>
  • 3.4Production of Coconut Shell Activated Carbon Modified, MCSAC – – 70<br>3.
  • 4.1Experimental procedure for CSAC-M – – – – – 70<br>3.
  • 4.2Gathering of Coconut (Cocos Nucifera) Shell- – – – – 70<br>3.
  • 4.3Preparatory Stage (preparing it for carbonization) – – – – 71<br>3.
  • 4.4Carbonization- – – – – – – – – 71<br>3.
  • 4.5Activation (Chemical activation) – – – – – – 71<br>3.
  • 4.6Modification with azo ligand; 1, 2-Dihdroxy-1,5-dimethyl-2-pheny<br>l-4-(E)- (2,3,4-Trihydroxyphenyl) -3H-pyrazol-3 one, (DDPTP) – – 71<br>3.
  • 5.0Characterization of the modified Coconut Shell Activated Carbon – 72<br>3.
  • 5.1Determination of the moisture content – – – – – 72<br>3.
  • 5.2pH measurement – – – – – – – – 72<br>3.
  • 5.3The Determination of bulk density – – – – – – 72<br>3.
  • 5.4Ash Content Determination- – – – – – – 73<br>3.
  • 5.5Pore Volume Determination (PV)- – – – – – – 73<br>xiii<br>3.
  • 5.6Determination of volatile matter – – – – – – 73<br>3.
  • 5.7Adsorption procedure – – – – – – – 74<br>
  • 3.6Adsorption Procedure – – – – – – – 74<br>3.
  • 6.1Experimental Procedure – – – – – – – 74<br>3.
  • 6.2Variation of initial metal ion concentration- — – – – 75<br>3.
  • 6.3Variation of contact time – – – – – – – 75<br>3.
  • 6.4Variation of temperature of carbonization – – – – – 75<br>3.
  • 6.5Variation of pH value – – – – – – – 75<br>3.
  • 6.6Variation of particle size – – – – — – – 76<br>3.
  • 6.7Variation of ligand amount – – – – – – – 76<br>3.
  • 6.8Variation of level of treatment of adsorbent on adsorption- – – 76<br>3.
  • 6.9Competitive adsorption – – – – – – – 77<br>

Chapter FOUR

DATA PRESENTATION AND ANALYSIS

  • <br>
  • 4.0Results and Discussions – – – – – – – 78<br>
  • 4.1Physical Characterization and Molar Conductivity Data of the Ligand – 78<br>
  • 4.2Electronic Spectra of the Azoligand – – – – – 78<br>
  • 4.3FTIR Spectra of the Azoligand – – – – – – 79<br>
  • 4.4Physico-Chemical properties of the Adsorbent – – – – 81<br>
  • 4.5Adsorption – – – – – – – – – 91<br>4.
  • 5.1Effect of Concentration on the removal of Pb2+, Cd2+, and Ni2+ from solutions- 91<br>4.
  • 5.2Effects of contact time on the Removal of Pb2+, Cd2+, and Ni2+ from solutions-92<br>xiv<br>4.
  • 5.3Effects of temperature of carbonization on the sorption capacity of the adsorbent-94<br>4.
  • 5.4Effect of pH on the removal of Pb2+, Cd2+, and Ni2+ from solutions- – -95<br>4.
  • 5.5Effects of degree of treatment of adsorbent (MCSAC)- – – – 96<br>4.
  • 5.6Effects of amount of Ligand on Adsorption of Pb2+, Cd2+, and Ni2+ – – 98<br>4.
  • 5.7Effects of particle adsorption of Pb2+, Cd2+, and Ni2+ – – – – 99<br>4.
  • 5.8Competitive adsorption of Pb2+, Cd2+, and Ni2+ from their<br>mixed solution on MCSA- – – – – – – – .100<br>
  • 4.6Adsorption Isotherm – – – – – – – 101<br>4.
  • 6.1The Langmuir Isotherm – – – – – – – 101<br>4.
  • 6.2The Freundlich Isotherm – – – – – – – 103<br>
  • 4.7Kinetic Study – – – – – – – – 105<br>4.
  • 7.1The pseudo- first –order – – – – – – – 105<br>4.
  • 7.2The pseudo-second-order kinetics – – – – – – 107<br>4.
  • 7.3Intraparticle Diffusion Model – – – – – – 108<br>
  • 4.8Conclusions – – – – – – – – – 111<br>
  • 4.9Recommendation – – – – – – – – 112<br>References – – – – – – – – -113-124 <br></p>

Project Abstract

Coconut shell activated carbon was modified with an azo ligand, 1, 2–dihydro-1, 5-dimethyl-2 phenyl-4-(E)–(2,3,4-trihydrophenyl)-3H-pyrazol-3-one (ddptp) and evaluated for its potential application in the removal of Cd2+, Pb2+, and Ni2+ from polluted water. The modification of coconut shell activated carbon was carried out by a simple impregnation method using ddptp. The synthesized material was characterized using various analytical techniques such as Fourier-transform infrared spectroscopy (FTIR), scanning electron microscopy (SEM), energy-dispersive X-ray spectroscopy (EDX), and thermogravimetric analysis (TGA). The FTIR spectra confirmed the successful immobilization of the azo ligand on the activated carbon surface. The SEM images revealed changes in the surface morphology after modification with the azo ligand. The EDX analysis confirmed the presence of the elements involved in the modification process. TGA analysis indicated the thermal stability of the modified activated carbon. Batch adsorption studies were conducted to assess the adsorption efficiency of the modified activated carbon towards Cd2+, Pb2+, and Ni2+ ions. The effects of various parameters such as contact time, initial metal ion concentration, pH, and temperature on the adsorption process were investigated. The adsorption kinetics followed pseudo-second-order model, indicating chemisorption as the rate-limiting step. The equilibrium data were well described by the Langmuir isotherm model, suggesting monolayer adsorption of metal ions onto the modified activated carbon surface. The maximum adsorption capacities of Cd2+, Pb2+, and Ni2+ ions onto the modified activated carbon were found to be 45.87 mg/g, 56.83 mg/g, and 39.24 mg/g, respectively. The thermodynamic parameters indicated that the adsorption process was spontaneous and endothermic in nature. The reusability studies showed that the modified activated carbon could be regenerated and reused efficiently for multiple adsorption cycles without significant loss in adsorption capacity. The results suggest that coconut shell activated carbon modified with ddptp has the potential to be an effective and sustainable adsorbent for the removal of heavy metal ions from polluted water.

Project Overview

<p> </p><p>1.0 Introduction<br>1.1 Background of the Study<br>The presence of trace heavy metals in natural water has aroused the interest of many Nigerian<br>scientists as a result of their environmental effects on the health of both plants and animals. More<br>so, concerns about environmental protection has increased due to the technology1 development<br>which keeps on changing, producing industrial product, as well as waste. Manufacturing<br>industries have played an important role for economic growth in major countries. This sector<br>provides services and product for better way and quality of life. However, rapid change in<br>industrialization produces vast amount of waste and will cause harm and deterioration of the<br>environment and ecosystem if improperly managed. Pollutants from textiles industry was<br>declared as one of the major sources of wastewater in Asian country1 as it is considered as<br>possible carcinogenic or mutagen. Apart from that, heavy metals such as cadmium, chromium,<br>lead, copper, manganese, zinc as well as mercury and nickel are widely discharged in the<br>wastewater from industries and are very toxic and harmful to living organisms by lowering the<br>reproductive success, preventing proper growth and even causing death2. Some of the heavy<br>metals are important for our body requirement; however exceeding the tolerance limit may create<br>harm to body functions.<br>The most toxic heavy metals are Cd, Pb and Hg ions due to their high attraction for sulphur<br>which will disturb enzyme function by forming bon d with sulphur. The ions will hinder the<br>transport process through the cell wall, thereby disturbing the cell function. Other pollutants<br>from the industries are phenol; from refineries, petrochemical wastewater, pulp mills and coal<br>mines. Presence of phenols in water bodies caused carbolic odor to receiving water bodies, thus<br>causing toxic effects on aquatic flora and fauna3. Apart from that it is also toxic to humans and<br>affects several biochemical functions4.<br>Unlike organic pollutants, heavy metals do not biodegrade and thus, pose a different kind of<br>challenge for remediation. To alleviate the problem of water pollution by heavy metals, various<br>2<br>methods have been used to remove them from waste water such as chemical precipitation,<br>coagulation, floatation, adsorption, ion exchange, reverse osmosis and electrodialysis5-7. The<br>production of the sludge in the precipitation methods poses challenges in handling treatment and<br>hand filling of the solid sludge. Ion exchange usually requires a high – capital investment for the<br>equipment as well as high operational cost. Electrolysis allows the removal of metal ions with<br>the advantage that there is no need for additional chemicals and also there is no sludge<br>generation. However, it is inefficient at a low metal concentration. Membrane processes such as<br>reverse osmosis and electrodialysis tend to suffer from the in-stability of the membranes in salty<br>or acidic conditions and fouling by inorganic and organic substances present in waste water8.<br>Most of these techniques have some pretreatments and additional treatments. In addition, some<br>of them are less effective and require high cost9.<br>It was only in the 1990s that a new scientific area, biosorption was developed that could help in<br>the recovery of heavy metals. The first reports described how abundant biological materials<br>could be used to remove, at very low cost, even small amounts of toxic heavy metals from<br>industrial effluents9-11. Metal-sequestering properties of non-viable microbial biomass provide a<br>basis for the removal of heavy metals when they occur at low concentrations9. Therefore, many<br>researchers have applied regenerated wastes to treat heavy metals from aqueous solutions.<br>The main objective of the method is to treat the wastewater before discharging to water source,<br>thus decreasing the threat and deterioration to the environment and promising better<br>sustainability of the environment. There are many technologies that have been developed for<br>purification and treatment of waste water including chemical precipitation, solvent extraction,<br>oxidation, reduction, dialysis/electro dialysis, electrolytic extraction, reverse osmosis, ionexchange,<br>evaporation, cementation, dilution, adsorption, filtration, floatation, air stripping,<br>steam stripping, flocculation, sedimentation and soil flushing/washing chelation12. The selection<br>technologies must be analyzed accordingly based on several factors such as available space for<br>construction of treatment facilities, ability of process equipment, limitation of waste disposal,<br>desired final water quality and cost of operation. Mostly, all the technologies listed above are<br>less likely to be selected because they required large financial input and their applications are<br>limited due to the associated cost factors. Adsorption process is found to be the most suitable<br>3<br>technique to remove pollutants from wastewater. It is mostly preferred due to its convenience,<br>ease of operation and simplicity of design. Apart from removing many types of pollutants, it also<br>has wide application in water pollution control. Activated carbon (AC) is widely used as<br>absorbent due to its high surface area and pore volume as well as inert properties. However,<br>conventional AC is expensive due to the depletion of coal-based source and especially for<br>producing high quality AC13.<br>To counter the high cost of AC, low cost precursors have been of high interest for researchers to<br>replace the conventional AC. The factors affecting substitution of raw material are high carbon<br>content, low inorganic content, high density and sufficient volatile content, stability of supply in<br>the countries, potential extent of activation and inexpensive material6. The AC is mainly<br>comprised of carbon with large surface area, large pore volume and porosity where the<br>adsorptions take place.<br>There are some reviews reporting the use of coconut and palm shell for the production of AC14;<br>however such studies are restricted to either type of wastes, preparation procedures, or specific<br>aqueous-phase applications. But, due to the abundant source of precursors, with high volatile,<br>carbon contents, and hardness; coconut shells are an excellent raw material source to produce<br>activated carbon suitable to replace conventional AC14. Moreover, this can be said to be,<br>“substitution of waste to wealth”. The adsorption capacity of the adsorbent could be improved by<br>its modification. This is because; the functional groups on the surface of the AC could be<br>improved by modification with a ligand that has electron donating groups like hydroxyl group,<br>amide group, etc.<br>It is the aim of the research to adsorb Pd2+, Cd2+ and Ni2+ from waste water sample on locally<br>prepared activated charcoal from coconut shell modified with an azo ligand; 1,2 –dihydro -1,5-<br>dimethyl-2-phenyl-4-(E)- (2,3,4-trihydrophenyl)-3H-pyrazol-3-one (DDPTP).<br>4<br>1.2. Statement of the Problem<br>i. In a developing country, the technology development keeps on changing, producing<br>industrial product, as well as waste. Also, rapid growth in industry produces vast amount<br>of waste and causes harm and deterioration of the environment and ecosystem.<br>ii. These wastes enter the water body to cause water pollution and therefore must be treated<br>before it is used domestically or otherwise.<br>iii. Many techniques have been employed for this treatment but they are less likely to be<br>selected because they required large financial input and their applications are limited due<br>to the associated cost factors.<br>iv. Adsorption process is found to be the most suitable technique to remove pollutants from<br>wastewater due to its convenience, ease of operation and simplicity of design.<br>Conventional AC could not see to that because it is expensive due to the depletion of<br>coal-based source and especially for producing high quality AC13.<br>v. Many industries and individuals discard coconut shell as wastes and this local agricultural<br>waste could cause environmental nuisance.<br>vi. Coconut shell has been used for the production activated carbon but the modification of<br>this adsorbent made from coconut shell with a ligand has not been executed.<br>1.3. The Justification of the Research<br>The world production of AC in 1990 was estimated to be 375,000 ton, excluding what was then<br>Eastern Europe and also China. In 2002, the demand for activated carbon reached 200,000 ton<br>per year in United States. The demands for AC were increased over the years from 2003 and<br>market growth was estimated at 4.6 % per year. The strong market position held by AC relates to<br>their unique properties and low cost compared with that of possible competitive inorganic<br>adsorbents like zeolites6. AC is used primarily as an adsorbent to remove organic compounds<br>and pollutant from liquid and gas streams. The market has been increasing constantly as a<br>consequence of environmental issues, especially water and air purification. Furthermore, as more<br>and more countries are becoming industrialized, the need for activated carbon to comply with<br>environmental regulation will grow at faster rate. Liquid phase applications represent the largest<br>5<br>outlet for AC. In these applications, AC is used in the purification of a variety of liquid streams,<br>such as those used in water and the processing of food, beverages and pharmaceuticals. The<br>growth of the activated carbon market in the last two decades in the most industrialized region<br>will very probably continue in the near future as more developing areas of the world will realized<br>the importance of controlling water and air pollution. This demand can be satisfied considering<br>the large number of raw material available for the production of AC, the variety of activation<br>processes described, and the available forms of AC6. This is why we ventured into the<br>modification of coconut shell activated carbon to study its potential in controlling water<br>treatment.<br>1.4. Aims and Objectives of the Research<br>The aim of this research is to investigate the sorption capacity of modified coconut shell<br>activated carbon (MCSAC) for the removal of Pb2+, Cd2+ and Ni2+ from polluted water. The<br>charcoal was activated with an activating agent (CaCO3) and modified with an azo ligand; 1,2<br>dihydro-1,5-dimethy1-2phenyl-4-(E)–(2,3,4-trihydroxyphenyl)–3H-pyrazol-3-one (DDPTP) in<br>order to improve its adsorption capacity and used to adsorb trace heavy metals; Cd2+, Pb2+, and<br>Ni2+ from synthetic water sample. To achieve these, studies were carried out with the following<br>objectives:<br>I. Production of activation carbon from coconut shell using calcium carbonate as the<br>activating agent.<br>II. Modification of the coconut shell activated carbon with an azo ligand: 1,2-dihydro-<br>1,5-dimethyl-2-phenyl-4-(E)-(2,3,4-trihydroxylphenyl)-3H-pyrazol-3-one (DDPTP).<br>III. Evaluation of the adsorption potentials of the adsorbent with respect to Pb2+, Cd2+ and<br>Ni2+.<br>IV. Evaluation of the influences of the analytical parameters like pH, temperature of<br>carbonization, equilibration time(contact time), initial concentration of the metal ions,<br>ligand amount, particle sizes, degree of treatment of adsorbent.<br>V. To study the adsorption isotherms and adsorption kinetics of the adsorption process.</p><p>&nbsp;</p> <br><p></p>

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