TABLE OF CONTENTS
Abstract
CHAPTER ONE
1.0 Introduction
1.1 Background of Study
1.2 Statement of Problems
1.3 Research Objectives
1.4 Research Question
1.5 Research Hypothesis
1.6 Scope of Study
1.7 Significance of study
1.8 Limitation of study
1.9 Definition of terms
CHAPTER TWO
2.0 Literature Review
CHAPTER THREE
3.0 Research methodology
3.1 Research Design
3.2 Population of study
3.3 Sampling Design and Procedure
3.4 Data Collection Instrument
3.5 Administration of Data Collection Instrument
3.6 Methods of data analysis
CHAPTER FOUR
4.0 Data Presentation and Analysis
4.1 Data Presentation
4.2 Test of Hypothesis
CHAPTER FIVE
5.0 Summary, Conclusion and Recommendation
5.1 Summary
5.2 Conclusion
5.3 Recommendation
References
Questionnaire
ABSTRACT
Palm Oil processing yields a considerable quantity of palm kernel shell (PKS) and mesocarp fruit fiber (MFF). This has been predominantly used as fuel through direct combustion which is inefficient and polluting. Better grade fuel could be derived through torrefaction. The objectives of the work therefore was to determine the optimum parameters for the conversion of palm kernel shell (PKS) and mesocarp fruit fiber (MFF) to high grade fuel via torrefaction. Samples of
PKS and MFF were torrefied with a temperature range of 200°C to 350°C at the step of 30°C. The torrefied product yield were determined by weighing, proximate, ultimate analysis of the torrefied product were determined using A.O.A.C. method. The higher heating value was calculated using Dulong Petit. Percentage torrefied product decreases as the reaction temperature increases, from 71.70% to 56.32% for 200°C to 350°C. The higher heating value ranges from 8607.6MJ/Kg to 9510.4MJ/Kg for 200°C to 350°C respectively. Palm kernel shell has higher heating value when compared with mesocarp fruit fiber. PKS at 350°C had the highest value for HHV palm kernel shell and mesocarp fruit fibre torrefied.