Design, construction and performance evaluation of a fixed bed pyrolysis system
Table Of Contents
- <p> DECLARATION ii<br>CERTIFICATION iii<br>DEDICATION iv<br>ACKNOWLEDGEMENT v<br>ABSTRACT vi<br>LIST OF FIGURES xi<br>LIST OF TABLES xiii<br>LIST OF PLATE xiv<br>LIST OF APPENDICES xv<br>NOMENCLATURE xvi<br>
Chapter ONE
INTRODUCTION
- <br>
- 1.1Background of the Study 1<br>
- 1.2Statement of the Research Problem 2<br>
- 1.3The Present Research 3<br>
- 1.4Aim and Objectives of the Research 3<br>
- 1.5Justification of the Study 3<br>
- 1.6The Scope of the Research 4<br>
Chapter TWO
LITERATURE REVIEW
- <br>
- 2.1History of Pyrolysis 5<br>
- 2.2Principle of Pyrolysis 5<br>2.
- 2.1Slow Pyrolysis 7<br>2.
- 2.2Fast Pyrolysis 8<br>2.
- 2.3Flash Pyrolysis 9<br>
- 2.3Pyrolysis Reactor 9<br>viii<br>2.
- 3.1Fixed Bed Reactor 10<br>2.
- 3.2Fluidized Bed Reactor 11<br>2.3.
- 2.1Bubbling Fluidized Bed Reactor 11<br>2.3.
- 2.2Circulating Fluidized Bed Reactor 12<br>2.
- 3.3Ablative Reactor 13<br>2.
- 3.4Vacuum Pyrolysis Reactor 14<br>2.
- 3.5Rotating Cone Reactor 15<br>2.
- 3.6Pyros Reactor 16<br>2.
- 3.7Auger Reactor 17<br>2.
- 3.8Plasma Reactor 18<br>2.
- 3.9Microwave Reactor 19<br>2.
- 3.10Solar Reactor 20<br>
- 2.4Factors Affecting Pyrolysis of Biomass 21<br>2.
- 4.1Feedstock Composition 22<br>2.
- 4.2Feedstock Preparation 23<br>2.
- 4.3Pyrolysis Temperature Control 24<br>2.
- 4.4Residence Time 26<br>2.
- 4.5Moisture Content 26<br>
- 2.5Biomass 27<br>2.
- 5.1Biomass Conversion Technology 28<br>2.
- 5.2Feed stock/ material background 29<br>
- 2.6Fourier Transform infra-red (FTIR) 30<br>
- 2.7Gas Chromatography/ Mass Spectroscopy (GC-MS) 30<br>
- 2.8Review of related past works 31<br>
- 2.9Research gap 34<br>ix<br>
Chapter THREE
SYSTEM DESIGN AND IMPLEMENTATION
- MATERIALS AND METHODS<br>
- 3.1Materials 35<br>3.
- 1.1List of Materials 35<br>
- 3.2Methods 36<br>3.
- 2.1Description of the fixed pyrolysis system 36<br>3.
- 2.2Design Theory and Equation 37<br>3.2.2.1Initial design parameters 37<br>3.2.
- 2.2Stresses in the fixed bed reactor 38<br>3.2.
- 2.3Reactor Thickness 39<br>3.2.
- 2.4Insulation 39<br>3.2.2.4.1Insulation Thickness 39<br>3.2.
- 2.5Design of the Reactor 42<br>3.2.
- 2.6Design of the Condenser 45<br>3.2.
- 2.7Design calculation of the fixed bed pyrolysis system 48<br>3.
- 2.3Construction of the fixed bed pyrolysis system 51<br>3.
- 2.4Assembly of the pyrolysis system 53<br>3.
- 2.5Experimental procedure 55<br>3.2.
- 5.1Preparation of Feedstock 55<br>3.2.
- 5.2Operational procedures of the fixed bed pyrolysis system 55<br>3.
- 2.6Characterization of Palm kernel Shells (PKS) 56<br>3.2.
- 6.1Proximate analysis of PKS 56<br>3.2.
- 6.2Ultimate analysis of palm kernel shell 57<br>3.2.
- 6.3Determination of the calorific value of the palm kernel shell 57<br>3.
- 2.7Performance evaluation of the fixed bed pyrolysis system 58<br>3.
- 2.8Effect of pyrolysis parameters 59<br>3.2.
- 8.1Effect of particle size 59<br>x<br>3.2.
- 8.2Effect of temperature 59<br>3.2.
- 8.3Effect of running time 59<br>3.
- 2.9Characterization of bio-oil 59<br>3.2.
- 9.1Ultimate analysis of the bio-oil 60<br>3.2.
- 9.2Determination of the calorific value of the bio-oil 60<br>3.2.
- 9.3Fourier Transform infra-red (FTIR) 60<br>3.2.
- 9.4Gas Chromatography/ Mass Spectroscopy (GC-MS) 60<br>
Chapter FOUR
SYSTEM TESTING AND EVALUATION
- RESULTS AND DISCUSSION<br>
- 4.1Characterization of palm kernel shells (PKS) 62<br>
- 4.2Variation of pyrolysis parameters 63<br>4.
- 2.1Effect of Particle Size 63<br>4.
- 2.2Effect of Temperature 65<br>4.
- 2.3Effect of Running time 67<br>
- 4.3Performance evaluation of the fixed bed pyrolysis system 68<br>
- 4.4Characterization of bio-oil product 69<br>4.
- 4.1Ultimate analysis of the bio-oil 69<br>4.
- 4.2FTIR analysis of bio-oil 69<br>4.
- 4.3GCMS analysis of the Bio-oil 70<br>
- 4.5Cost Estimate 72<br>
Chapter FIVE
SUMMARY, CONCLUSION AND RECOMMENDATIONS
- S AND RECOMMENDATIONS<br>
- 5.1Conclusions 74<br>
- 5.2Recommendations 75<br>
- 5.3Significant Contributions 75<br>REFRENCES 77<br>APPENDICES 86<br>xi <br></p>
Project Abstract
<p> A fixed bed pyrolysis system has been designed and constructed for obtaining liquid fuel<br>from palm kernel shell. The major components of the system are fixed bed reactor and<br>condensate unit. The palm kernel shell in particle form was pyrolized in an externally<br>heated 90mm diameter and 360mm high fixed bed reactor. The reactor is heated by means<br>of a rectangular shape manual forge blower with charcoal as the energy source. The<br>products are char, oil and gas. The parameters varied are feed particle size, reactor bed<br>temperature and running time. The reactor bed temperature was found to influence the<br>product yields. The maximum liquid yield was 38.67wt % at 4500C for a feed particle size<br>of 1.18mm with a running time of 95minutes. The maximum char yield was 70.67wt% at<br>5500C for a feed particle size of 5mm with a running time of 120minutes. The calorific<br>value of the palm kernel shells (22.81 MJkg-1) and bio-oil (43.19MJkg-1) were determined.<br>The reactor efficiency was evaluated at various temperatures. Maximum efficiency of<br>73.21% indicated that the reactor is efficient enough to produce bio-oil. The bio-oil<br>products were analysed by Fourier Transform Infra-red Spectroscopy (FTIR) and Gas<br>Chromatography Mass Spectrometry (GCMS). The FTIR analysis showed that the bio-oil<br>was dominated by phenol and its derivatives. The phenol, 2-methoxy-phenol and 2, 6-<br>dimethoxyl phenol that were identified by GCMS analysis are highly suitable for<br>extraction from bio-oil as value-added chemicals. The highly oxygenated oils need to be<br>upgraded in order to be used in other applications such as transportation fuels.<br>vii <br></p>
Project Overview
<p>
INTRODUCTION<br>1.1 Background of the Study<br>Uninterrupted energy supply is a vital issue for all countries today. Future economic<br>growth crucially depends on the long-term availability of energy from sources that are<br>affordable, accessible, and environmentally friendly. Security, climate change, and public<br>health are closely interrelated with energy (Ramchandra and Boucar, 2011). The standard<br>of living of a given country can be directly related to the per capita energy consumption.<br>The recent world’s energy crisis is due to two reasons: the rapid population growth and the<br>increase in the living standard of societies. The per capita energy consumption is a measure<br>of the per capita income as well as a measure of the prosperity of a nation (Chikaire et al.,<br>2015).<br>Energy supports the provision of basic needs such as cooked food, a comfortable living<br>temperature, lighting, the use of appliances, piped water or sewerage, essential health care<br>(refrigerated vaccines, emergency and intensive care), educational aids, communication<br>(radio, television, electronic mail, the World Wide Web), and transport. Energy also fuels<br>productive activities including agriculture, commerce, manufacturing, industry, and<br>mining. Conversely, lack of access to energy contributes to poverty and deprivation and<br>can contribute to the economic decline. Energy and poverty reduction are not only closely<br>connected with each other, but also with the socioeconomic development, which involves<br>productivity, income growth, education, and health (Nnaji et al., 2010).<br>The high rate of extracting the crude oil from the earth-crust demands for an alternative<br>and dependable source of obtaining energy (Rajput, 2005). This alternative is the energy<br>derived via pyrolysis (a thermal decomposition process that occurs at moderate<br>2<br>temperatures with a high heat transfer rate to the biomass particles and a short hot vapour<br>residence time in the reaction zone) of agricultural and forest residues (generally called<br>biomass). Biomass has been recognized as a major renewable energy source to supplement<br>declining fossil fuel sources of energy. It is the most popular form of renewable energy and<br>currently biofuel production is becoming very much promising. Transformation of energy<br>into useful and sustainable forms that can fulfil and suit the needs and a requirement of<br>human beings in the best possible way is the common concern of the scientists, engineers<br>and technologists. In this contest, bio fuels can be realised through fixed bed pyrolysis<br>system using palm kernel shells as biomass. Fixed bed pyrolysis is more attractive among<br>various thermo-chemical conversion processes because of its simplicity and higher<br>conversion capability of biomass and solid wastes to yield char, liquid and gases (Hossain<br>et al., 2014).<br>1.2 Statement of the Research Problem<br>From the literature reviewed, it is obvious that a lot of research works have been conducted<br>on fixed bed pyrolysis system powered by electric heater. However, it is obvious from the<br>review that fixed bed pyrolysis system powered by electric heater can only be efficiently<br>used where there is steady electricity supply which is the major limitation of this system<br>(especially in Nigeria).<br>The use of stainless steel for the construction of the reactor has a significant effect on the<br>cost of the pyrolysis products. Therefore, there is a need to source for alternative material<br>to minimize the cost at optimum production.<br>3<br>1.3 The Present Research<br>The current work focuses on the design, construction and performance evaluation of a<br>fixed bed pyrolysis system, which will use palm kernel shells to produce bio-fuels. The<br>bio-oil produced can then be used to generate heat and power from small stationary diesel<br>engines, gas turbines and boilers. The agricultural by-products include maize cobs,<br>groundnut shells, palm kernel shells, rice and millet husks, millet stalks, sorghum stalks,<br>sugar cane bagasse, maize stalks and cotton stalks among others. However, this research<br>will focus on palm kernel shells because of its availability.<br>1.4 Aim and Objectives of the Research<br>The aim of this research is to design and construct an externally heated fixed bed pyrolysis<br>system for the production of alternative liquid oil from palm kernel shells.<br>Therefore, the specific objectives of this research are to:<br>i. design a fixed bed pyrolysis system.<br>ii. construct the fixed bed pyrolysis system.<br>iii. evaluate the performance of the fixed bed pyrolysis system to determine its<br>effectiveness in bio-oil production.<br>iv. characterise the bio-oil produced from the fixed bed pyrolysis system using<br>FTIR and GCMS analyses.<br>1.5 Justification of the Study<br>Nigeria is blessed with abundant renewable energy resources such as hydroelectric, solar,<br>wind, tidal, and biomass, there is a need to harness these resources and chart a new energy<br>future for Nigeria. To enhance the developmental trend in the country, there is every need<br>to support the existing unreliable energy sector with a sustainable source of power supply<br>through pyrolysis of biomass.<br>4<br>There are several benefits of introducing electricity to rural communities. While obvious<br>reasons include social gains like lightening, cooking and water pumping, electricity will<br>help to stem the flow of rural-urban migration which is a common problem in many<br>developing countries like Nigeria. Introduction of electricity also helps to provide<br>productive employment in rural areas thereby creating a positive impact on economic as<br>well as social growth. Fixed bed pyrolysis when combined with a boiler can provide<br>efficient and affordable source of energy thereby boosting rural education and<br>development, since it uses agricultural waste as a fuel source. Bio-oil generated can either<br>be used for electricity production in a gas turbine or generate steam in a boiler.<br>1.6 The Scope of the Research<br>The scope of this research is:<br>i. Design, construction and performance evaluation of a fixed bed pyrolysis<br>system, which will use palm kernel shells as feed materials to produce biofuels.<br>ii. The emphasis of the study is on the production of a liquid fuel from 1.5kg per<br>sample of palm kernel shells using fixed bed pyrolysis system. The char<br>product will be also quantified.<br>5
<br></p>