Synthesis and characterization of zeolite and its application in adsorption of nickel from aqueous solution
Table Of Contents
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</p><p>Title page .. .. .. .. .. .. .. .. .. i<br>Approval page .. .. .. .. .. .. .. .. .. ii<br>Certification page .. .. .. .. .. .. .. .. .. iii<br>Dedication .. .. .. .. .. .. .. .. .. iv<br>Acknowledgment .. .. .. .. .. .. .. .. .. v<br>Abstract vi<br>Table of contents .. .. .. .. .. .. .. .. .. vii<br>List of table .. .. .. .. .. .. .. .. .. .. x<br>List of figure .. .. .. .. .. .. .. .. .. xii<br>List of abbreviations .. .. .. .. .. .. .. .. .. xiv<br>
Chapter ONE
<br>1.0 Introduction .. .. .. .. .. .. .. .. .. .. 1<br>1.1 Background of study .. .. .. .. .. .. .. .. 2<br>1.2 Statement of problem .. .. .. .. .. .. .. .. 3<br>1.3 Objectives of the study .. .. .. .. .. .. .. .. .. 3<br>1.4 Justification .. .. .. .. .. .. .. .. .. .. 3<br>
Chapter TWO
<br>2.0 Literature review .. .. .. .. .. .. .. .. .. 4<br>2.1 Natural zeolites .. .. .. .. .. .. .. .. .. 6<br>2.2 Synthetic zeolite .. .. .. .. .. .. .. .. .. 9<br>2.2.1 Synthetic zeolite from natural materials .. .. .. .. .. .. 13<br>2.2.2 Synthetic zeolite from waste materials .. .. .. .. .. .. 15<br>2.2.2.1 Zeolites from coal fly ash (CFA) .. .. .. .. .. .. 15<br>2.2.2.2 Zeolite from municipal solid waste incineration ash (MSWIA) .. .. .. 16<br>2.2.2.3 Zeolites from oil shale ash (OSA) .. .. .. .. .. .. .. 17<br>viii<br>2.2.2.4 Zeolite from rice husk ash (RHA) .. .. .. .. .. .. 17<br>2.2.2.5 Zeolite from other wastes .. .. .. .. .. .. .. 18<br>2.2.2.6 Modified natural and synthetic zeolites .. .. .. .. .. .. 19<br>2.3 Application of zeolite: (waste) water treatment .. .. .. .. .. 20<br>2.3.1 Heavy metals removal .. .. .. .. .. .. .. .. 20<br>2.3.1.1. Industrial wastewater sources .. .. .. .. .. .. .. 25<br>2.3.1.2 Adsorption of heavy metals on adsorbent .. .. .. .. .. 26<br>2.3.1.3 Mechanisms of heavy metals removal from industrial wastewater .. .. 27<br>2.3.2 Water softening .. .. .. .. .. .. .. .. .. 28<br>2.3.3 Ammonia removal .. .. .. .. .. .. .. .. .. 30<br>2.3.4 Radioactive species removal .. .. .. .. .. .. .. 34<br>2.3.5 Removal of inorganic anions .. .. .. .. .. .. .. 36<br>2.3.6. Organic compounds removal .. .. .. .. .. .. .. 37<br>2.3.6.1 Dyes removal .. .. .. .. .. .. .. .. .. 39<br>2.3.6.2 Micro organism capturing .. .. .. .. .. .. .. 38<br>2.3.6.3 Removal of others organics .. .. .. .. .. .. .. 41<br>2.4 Permeable reactive barriers (PRB) .. .. .. .. .. .. .. 41<br>2.5 Sea Water desalination .. .. .. .. .. .. .. .. 42<br>2.6 Adsorption isotherms .. .. .. .. .. .. .. .. 44<br>
Chapter THREE
<br>3.0 Experimental .. .. .. .. .. .. .. .. .. .. 46<br>3.1 General .. .. .. .. .. .. .. .. .. .. 46<br>3.1.1Synthesis of zeolite .. .. .. .. .. .. .. .. .. 47<br>3.1.2 Effect of pH .. .. .. .. .. .. .. .. .. 49<br>ix<br>3.1.3 Effect of temperature .. .. .. .. .. .. .. .. 49<br>3.1.4 Effect of adsorbent concentration .. .. .. .. .. .. 50<br>3.1.5 Effect of contact time .. .. .. .. .. .. .. .. 50<br>
Chapter FOUR
<br>4.0 Results and discussion .. .. .. .. .. .. .. .. 51<br>4.1 Scanning electron microscopy … …. … .. … .. .. … .. .. .. 51<br>4.2 X-ray diffraction .. …. .. .. .. .. .. .. .. .. .. .. 53<br>4.3 Effect of pH .. .. .. .. .. .. .. .. .. 55<br>4.4 Effect of temperature .. .. .. .. .. .. .. .. .. 56<br>4.5 Effect of amount of adsorbent .. .. .. .. .. .. .. 57<br>4.6 Effect of contact time .. .. .. .. .. .. .. .. 60<br>4.7 Adsorption isotherms .. .. .. .. .. .. .. .. .. 61<br>4.8 Adsorption kinetics .. .. .. .. .. .. .. .. .. .. .. 62<br>
Chapter FIVE
<br>Conclusion .. .. .. .. .. .. .. .. .. .. 68<br>References .. .. .. .. .. .. .. .. .. .. 69<br>Appendix .. .. .. .. .. .. .. .. .. .. 80<br>x</p><p> </p>
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Project Abstract
Project Overview
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</p><p>1.0 Introduction<br>Zeolites are porous crystalline alumino-silicates of regular skeleton structures formed<br>by alternating silicon-oxygen and aluminum-oxygen tetrahedrons. Although only natural<br>zeolites were initially used, synthetic zeolites, due to their well-tailored and highlyreproducible<br>structures, have been used extensively as ion exchangers, adsorbents, separation<br>materials and catalyst1.The negative charges in aluminum-oxygen tetrahedron, which are not<br>rigidly fixed to the skeleton of zeolites, are compensated with cations, so they are capable of<br>interchanging. Silicon-oxygen and aluminum-oxygen tetrahedrons in the zeolites of the type<br>A, X and Y form a complex structural unit of cubooctahedron. The combination of such units<br>forms the structure of type A, X and Y [fig 7].. The difference between them consists in the<br>fact that they are interconnected by means of different number of member rings (i.e., eight<br>member rings (A), twelve member rings (X, Y). The chemical difference of zeolite is defined<br>by the ratio of Si/Al. For zeolite A this values is in the range of 0.95-1.051-3. Zeolites A, X<br>and Y are the most important ones to be used in pharmaceutical, petrochemical and detergent<br>industries.<br>Zeolites with different structure are known to be obtained by synthesis 2-7. They are<br>either synthesized from alumino-silicate hydrogel or by conversion of clay minerals. The<br>hydrogel can be prepared from different sources of silica and alumina, but the types of<br>starting materials and the method of mixing determine the structure of the resulting gel.<br>Moreover, the nature of the gel influences the rate of the subsequent crystallization, which<br>affects the particle size distribution, and the formation of impurities8. The general pathway<br>for zeolite synthesis follows a specific temperature gradient at low temperatures (<60 oC)<br>2<br>where the sources of aluminum, silicon and water are placed in solution and mixed until a gel<br>is formed9.<br>Figure 1: Structure of zeolite framework<br>1.1 Background of Study<br>The extremely fast growth of the world population in the last century, in addition to<br>the industrial revolution, reflected in a considerable rise in both fresh water consumption and<br>waste water production. Fresh water demand has already exceeded supply; and currently<br>special treatment is more and more often required in order to obtain drinking water of high<br>quality as well as to produce environmentally acceptable effluents.<br>Species of toxic heavy metals cause serious damage to the ecosystem and as a result<br>of this fact, there is an increase in research on processes for wastewater treatment3. Many of<br>the wastewater treatment processes are based on adsorptive properties or ion exchange of<br>some of these materials which immobilize the heavy metal species. Recently, various<br>materials of natural or synthetic origin, such as bagasse, coal ash, carbonates, phosphates and<br>zeolite have been tested for their sorption capacity.4 Zeolite are commonly used for sorption<br>of heavy metals due to their physical and chemical properties (thermal stability, defined<br>molecular structure and ion exchange capacity.<br>3<br>1.2 Statement of Problem<br>The presence of large quantities of toxic metals such as mercury, lead, cadmium,<br>zinc, nickel and others in water poses serious health risk to humans, and this threat puts the<br>scientific community under pressure to develop new methods of detecting and removing<br>toxic contaminants from wastewater in efficient and economically viable way. The<br>production of zeolite from chemical sources (Al and Si ) are expensive but have the<br>advantage of producing zeolites of high purity with highly engineered chemical and physical<br>properties suitable for some specific applications in pharmacy, electrochemistry,<br>photochemistry, nano technologies, industries as well as for academic research purposes. The<br>greatest challenge now is the need to develop low cost and efficient adsorbents for nickel ion<br>removal from wastewater.<br>1.3 Objectives of the Study<br>The objectives of this study are:<br>i. To synthesize zeolite from analytical grade chemical.<br>ii. To characterize the synthesized zeolite using spectroscopic techniques such as<br>XRD, SEM and AAS.<br>iii. To use the synthesized zeolite to adsorb nickel ion from aqueous solution.<br>iv. To study the effect of pH, temperature, contact time and adsorbent dosage in<br>nickel metal removal.<br>1.4 Justification of the Study<br>The wide range of zeolite applications and the need to synthesize zeolite with high<br>purity motivated this work.The study has proffered cheaper routes of making zeolite with<br>high purity and thereby showed that zeolite is a good adsorbent for wastewater treatment</p><p> </p>
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