Abstract

One of the main sources of activated carbon is biomass which can be transformed into char by pyrolysis. Apart from the obtaining coal, the pyrolysis of biomass can be used for the preparation of fuels, and this is why it is very important to determine its kinetic parameters for modelling. In the present research, the pyrolysis enthalpy of palm nut shells (Elaeis guineensis) was determined with the use of a differential scanning calorimetry study (DSC). To determine the kinetic parameters, the Not Reacted Core model was employed. This model considers that there is a heat and mass gradient between the furnace atmosphere and the interface formed during pyrolysis. To obtain the required data for the model, palm nut shells were submitted to pyrolysis in a Nichols furnace under reducing atmosphere. Samples were taken every 10 minutes to calculate char conversion. The experimental pyrolysis enthalpy resulted to be 301.81 J/g and then the monomeric units of cellulose, hemicellulose, and lignin were employed in order to determine the pyrolysis enthalpy per mole. The three biopolymers react with different mechanisms at different temperatures. The molecular weight resulted to be 172.38 g/mole, and the enthalpy for pyrolysis was 52.03 kJ/mol. For the application of the Not Reacted Core model, the amorphous char heat transfer coefficient was selected, and the value is 1.6 J/s·m·K. The reaction rate constant was 6.64 × 10−9 1/s assuming a first-order reaction, whereas the effective diffusion across the char layer was 4.83 × 10−7 m2/s.

Highlights

  • Cellulose and hemicellulose may have the same mechanisms of thermal decomposition. e mechanisms proposed for the pyrolysis of cellulose consider dehydration and International Journal of Chemical Engineering depolymerization reactions with breakdown of glycosidic bonds and bonds which produce tar, levoglucosan, furfural, and heterocyclic compounds as well as CO, CO2, CH4, CnHm, and H2 [8]. e coal is produced by low temperature dehydration reactions and secondary reactions of repolymerization

  • To determine the kinetic parameters, the Not Reacted Core model was employed. is model considers that there is a heat and mass gradient between the furnace atmosphere and the interface formed during pyrolysis. e molecular weight of palm kernels was estimated considering the chemical composition of the monomeric units within each biopolymer. erefore, glucose, p-coumaryl alcohol, coniferyl alcohol, and synapyl alcohol were considered for molecular weight calculation according to their percentage in weight within palm kernels

  • These gases diffuse through the char layer towards the external atmosphere. e relevance of these model lies in the incorporation of all the three known mechanisms that may occur during biomass pyrolysis: heat transfer, chemical reaction at the interface, and mass transfer

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Summary

Introduction

It should be noted that each lignocellulosic material to be used tends to vary enormously in its chemical composition As it is of general knowledge, biomass is composed of several components, and the three more representatives are cellulose, hemicellulose, and lignin [2]. Lignocellulosic materials that have a higher concentration of lignin will tend to show endothermic pyrolysis. Lignocellulosic materials have a lower concentration of lignin and a greater quantity of cellulose and hemicellulose, and they will show an exothermic behaviour during pyrolysis. E mechanisms proposed for the pyrolysis of cellulose consider dehydration and International Journal of Chemical Engineering depolymerization reactions with breakdown of glycosidic bonds and bonds which produce tar, levoglucosan, furfural, and heterocyclic compounds as well as CO, CO2, CH4, CnHm, and H2 [8]. According to the reaction mechanisms proposed by several authors, the carbonization reaction of palm nut shells can be simpli ed as follows: Cq(s) ⟶ Ch(s) + Gas(g)

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