THESIS
2014
xx, 209 pages : illustrations (some color) ; 30 cm
Abstract
Pyrolysis process is the thermal decomposition of carbonaceous materials in the absence of
oxygen into carbonaceous residues, liquid hydrocarbons and combustible gases. It is a
precursor to other thermochemical processes (gasification and combustion) and therefore very
important thermochemical process. Pyrolysis process is an efficient and effective method of
treating solid wastes but its large-scale utilization is still limited by certain factors. The major
factor is the high amount of energy used during the pyrolysis process and in order to make
pyrolysis a cost effective commercial energy process, there is need to explore different
approaches/strategies to reduce energy usage during the process. Another important
challenges with pyrolysis of solid wastes are the stability of...[
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Pyrolysis process is the thermal decomposition of carbonaceous materials in the absence of
oxygen into carbonaceous residues, liquid hydrocarbons and combustible gases. It is a
precursor to other thermochemical processes (gasification and combustion) and therefore very
important thermochemical process. Pyrolysis process is an efficient and effective method of
treating solid wastes but its large-scale utilization is still limited by certain factors. The major
factor is the high amount of energy used during the pyrolysis process and in order to make
pyrolysis a cost effective commercial energy process, there is need to explore different
approaches/strategies to reduce energy usage during the process. Another important
challenges with pyrolysis of solid wastes are the stability of certain products fraction and
composition of the solid waste feedstocks. Therefore, in this study, experimental, modelling
and optimisation of solid wastes pyrolysis were investigated and different operational
strategies were proposed towards solving the pyrolysis problem. Selected solid wastes
feedstocks such as bamboo waste, waste tyres, sawdust, empty fruit bunch (EFB) and plastics
(polystyrene and high density polyethylene) were employed in this research study.
In the experimental study, common thermal analysis techniques and laboratory scaled
pyrolysis unit were used to study the influence of particle size, pyrolysis temperature and
heating rates on selected solid wastes feedstocks. A mathematical model was developed in MATLAB using the parameters generated from the experimental study. This model describes
transiently the pyrolysis progress of particles subjected to specified pyrolysis conditions in a
pyrolysis reactor. The effect of the operating parameters on the pyrolysis progress was studied
using the model and some experiments were conducted to validate the model results. In
addition to the pyrolysis model, selected operating conditions were optimised with focus on
minimizing energy input for the pyrolysis reaction. The constraints and optimisation equations
depend on the operating strategy under consideration.
Therefore in this present study, three operational strategies to reduce the energy usage during
the pyrolysis of solid wastes were proposed. The operational strategies are operating
parameters studies and optimisation including mixed-size approach, multi-stage pyrolysis and
optimisation and co-pyrolysis/mixed-waste pyrolysis. The results and the design of the
various approaches are clearly stated in this thesis. These operational strategies were shown to
minimize the energy usage, improve the pyrolysis products quality, enhance the pyrolysis
process efficiency and can further help in designing the operation of pyrolysis process in a
large scale. Overall, the application of some or all the proposed strategies will help to make
pyrolysis of solid wastes more energy efficient and more profitable on a large scale.
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