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
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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
<br>1.0. Introduction – – – – – – – – 1<br>1.1 Background 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
<br>2.0 Literature Review – – – – – – – – .6<br>2.1 Review of some work Related to this Research – – – – 6<br>2.2 Heavy metals – – – – – – – – – 12<br>2.2.1 Beneficial Heavy Metals – – – – – – – 12<br>2.2.2 Toxic Heavy Metals – – – – – – – 13<br>2.2.3 Cadmium – – – – – – – – 13<br>2.2.4 Properties of cadmium – – – – – – 14<br>2.2.5 Applications – – – – – – – – 14<br>2.2.6 Health effects of Cadmium – – – – – – 15<br>2.2.7 Lead – – – – – – – – – 15<br>2.2.8 Properties of lead – – – – – – – 17<br>2.2.9 Applications – – – – – – – – 17<br>2.2.10 Health effects of lead – – – – – – – 18<br>2.2.11 Nickel – – – – – – – – 19<br>2.2.12 Properties of Nikel – – – – – – – 19<br>2.2.13 Applications – – – – – – – 20<br>2.2.14 Health effect of Nikel – – – – – – .20<br>2.3 Pollution by Cd2+, Ni2+ and Pd2+ – – – – – – 22<br>2.3.1 Cadmium in the environment – – – – – – 22<br>2.3.2 Environmental effects of cadmium – – – – – – 23<br>x<br>2.3.3 Lead in the environment – – – – – – 24<br>2.3.4 Environmental effects of lead – – – – – – 24<br>2.3.5 Nikel in the environment – – – – – – 25<br>2.3.6 Effects of nickel on the environment – – – – – 25<br>2.3.7 Atomic Absorption Spectroscopy (AAS) – – – – 26<br>2.4 Adsorption Mechanism – – – – – – 29<br>2.4.1 What is Adsorption? – – – – – – – 29<br>2.4.2 How Adsorption occurs – – – – – – 29<br>2.4.3 Adsorption occurs – – – – – – – 30<br>2.4.4 Adsorption in solids – – – – – – – 30<br>2.4.5 Facts about Adsorption Process – – – – – 31<br>2.4.6 Type of Adsorption – – – – – – – 32<br>2.4.7 Applications of Adsorption – – – – – – 35<br>2.4.8 Factors on which Adsorption Depends – – – – 37<br>2.5.0 Adsorption Isotherm – – – – – – – 38<br>2.5.1 The Langmuir isotherm – – – – – – 38<br>2.5.2 The Freundlick isotherm – – – – – – 39<br>2.6 Displacement of Adsorbed Metals by Competitive Ions in Solution – – 41<br>2.7 The Ligand; Azo Ligand – – – – – – 42<br>2.7.1 Definition – – – – – – – – 42<br>2.7.2 Diazotization – – – – – – – – 42<br>xi<br>2.7.3 Azo Coupling – – – – – – – 43<br>2.7.4 4-Amionantipyrine – – – – – – – 43<br>2.7.5 Properties of 4- Amionantipyrine – – – – – 43<br>2.7.6 Pyrogallol – – – – – – – – 44<br>2.7.7 Properties of pyrogallol – – – – – – 44<br>2.8 Activated Carbon – – – – – – – 45<br>2.8.1 Definition of activated Carbon – – – – – 45<br>2.8.2 Historical Development of Activated Carbon- – – – 46<br>2.8.3 Properties of Activated Charcoal – – – – – 47<br>2.8.4 Chemical properties of Activated Carbon – – – – 52<br>2.8.5 Classification – – – – – – – – 54<br>2.8.6 Applications of Activated Charcoal – – – – – 57<br>2.8.7 Factors in which Selection of Raw Material Depends on – – 61<br>2.8.8 The Coconut Shell – – – – – – – 61<br>2.8.9 Uses of Coconut Shell Activated Carbon and its Advantages<br>over other ACs – – – – – – – 64<br>2.8.10 Activation of Coconut Shell Carbon – – – – – 64<br>
Chapter THREE
<br>3.0 Materials and Methods – – – – – – – 66<br>3.1 Apparatus – – – – – – – – – 66<br>3.2 Preparation of Reagents – – – – – – – 66<br>xii<br>3.2.1 Reagents- – – – – – – – – – 66<br>3.2.2 Preparation of 0.5 Moldm-3 of CH3COOH (Acetic Acid) – – – 67<br>3.2.3 Preparation of 0.5 Moldm-3 of HNO3 – – – – – – 67<br>3.2.4 Preparation of 1000 ppm Pb(NO3)2 solution – – – – – 67<br>3.2.5 Preparation of 1000 ppm Cd(NO3)2 4H2O solution – – – – 67<br>3.2.6 Preparation of 1000ppm NiCl2. 6H2O solution – – – – 68<br>3.3. Synthesis of the Ligand – – – – – – – 68<br>3.4 Production of Coconut Shell Activated Carbon Modified, MCSAC – – 70<br>3.4.1 Experimental procedure for CSAC-M – – – – – 70<br>3.4.2 Gathering of Coconut (Cocos Nucifera) Shell- – – – – 70<br>3.4.3 Preparatory Stage (preparing it for carbonization) – – – – 71<br>3.4.4 Carbonization- – – – – – – – – 71<br>3.4.5 Activation (Chemical activation) – – – – – – 71<br>3.4.6 Modification 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>3.5.0 Characterization of the modified Coconut Shell Activated Carbon – 72<br>3.5.1 Determination of the moisture content – – – – – 72<br>3.5.2 pH measurement – – – – – – – – 72<br>3.5.3 The Determination of bulk density – – – – – – 72<br>3.5.4 Ash Content Determination- – – – – – – 73<br>3.5.5 Pore Volume Determination (PV)- – – – – – – 73<br>xiii<br>3.5.6 Determination of volatile matter – – – – – – 73<br>3.5.7 Adsorption procedure – – – – – – – 74<br>3.6 Adsorption Procedure – – – – – – – 74<br>3.6.1 Experimental Procedure – – – – – – – 74<br>3.6.2 Variation of initial metal ion concentration- — – – – 75<br>3.6.3 Variation of contact time – – – – – – – 75<br>3.6.4 Variation of temperature of carbonization – – – – – 75<br>3.6.5 Variation of pH value – – – – – – – 75<br>3.6.6 Variation of particle size – – – – — – – 76<br>3.6.7 Variation of ligand amount – – – – – – – 76<br>3.6.8 Variation of level of treatment of adsorbent on adsorption- – – 76<br>3.6.9 Competitive adsorption – – – – – – – 77<br>
Chapter FOUR
<br>4.0 Results and Discussions – – – – – – – 78<br>4.1 Physical Characterization and Molar Conductivity Data of the Ligand – 78<br>4.2 Electronic Spectra of the Azoligand – – – – – 78<br>4.3 FTIR Spectra of the Azoligand – – – – – – 79<br>4.4 Physico-Chemical properties of the Adsorbent – – – – 81<br>4.5 Adsorption – – – – – – – – – 91<br>4.5.1 Effect of Concentration on the removal of Pb2+, Cd2+, and Ni2+ from solutions- 91<br>4.5.2 Effects of contact time on the Removal of Pb2+, Cd2+, and Ni2+ from solutions-92<br>xiv<br>4.5.3 Effects of temperature of carbonization on the sorption capacity of the adsorbent-94<br>4.5.4 Effect of pH on the removal of Pb2+, Cd2+, and Ni2+ from solutions- – -95<br>4.5.5 Effects of degree of treatment of adsorbent (MCSAC)- – – – 96<br>4.5.6 Effects of amount of Ligand on Adsorption of Pb2+, Cd2+, and Ni2+ – – 98<br>4.5.7 Effects of particle adsorption of Pb2+, Cd2+, and Ni2+ – – – – 99<br>4.5.8 Competitive adsorption of Pb2+, Cd2+, and Ni2+ from their<br>mixed solution on MCSA- – – – – – – – .100<br>4.6 Adsorption Isotherm – – – – – – – 101<br>4.6.1 The Langmuir Isotherm – – – – – – – 101<br>4.6.2 The Freundlich Isotherm – – – – – – – 103<br>4.7 Kinetic Study – – – – – – – – 105<br>4.7.1 The pseudo- first –order – – – – – – – 105<br>4.7.2 The pseudo-second-order kinetics – – – – – – 107<br>4.7.3 Intraparticle Diffusion Model – – – – – – 108<br>4.8 Conclusions – – – – – – – – – 111<br>4.9 Recommendation – – – – – – – – 112<br>References – – – – – – – – -113-124
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Thesis Abstract
Thesis Overview
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</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> </p>
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