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Pyrolysis of plastic waste is the best way to manage the waste while producing biofuels which can be
improved to replace diesel. However, plastic thermal pyrolysis has certain limitations, such as the high
decomposition temperature. Co-pyrolytic techniques have received much attention to provide an
alternative way to dispose and convert plastic and lignocellulosic biomass waste into high-value added
products. In this work, pine sawdust (SD) co-pyrolysis with polypropylene (PP) and polystyrene (PS) was
investigated, which resulted in a decrease in the decomposition temperature. The main objectives of this
study are to build knowledge on the co-pyrolysis of mixed biomass and plastic waste using two model fitting (Criado and Coats–Redfern) methods. Co-pyrolysis behavior of pine sawdust, waste plastics, and
their blends was characterized using thermogravimetric analyzer (TGA). The data obtained from TGA
reveals the decomposition behavior of materials involved and their synergistic effect. This has been done
for each of the plastics, biomass, and their blends. Seven different co-pyrolysis tests were conducted using
(TGA) at a heating rate of 200C/min for different binary and ternary mixed compositions of polypropylene
(PP), polystyrene (PS), and pine saw dust (SD) were conducted. The Master plot of the Criado model was
used to determine the most suitable reaction mechanism. Then, the Coats-Redfern model was used to
efficiently obtain the kinetic parameters (Ea and A0), and the values of the activation energy (Ea) and
pre-exponential factor (A0) of waste plastics (PP and PS) and pine sawdust (SD) decomposition were
found to be 111.4,110.46 and 48.78kJ/mol respectively. The activation energy of the plastic
decomposition reaction was reduced to 99.35kJ/mol when plastics were mixed with sawdust. Simulation
of plastic and biomass co-pyrolysis process was modelled with the aid of Aspen HYSYS V10 to estimate
the bio-fuel yields from PS, PP and SD. Aspen HYSYS simulator was used to develop the steady state
model and to simulate the co-pyrolysis process with the above mentioned plastic and biomass blends.
PengRobinson thermodynamics model was employed as a fluid package of this simulation. The process
converts waste to fuel as a two stage process in an Aspen HYSYS Simulation Environment involving i) A
conversion of plastics and biomass wastes into Vapor-Liquid Fraction (VLF) with small quantity of char
residue using conversion reactor (Pyrolytic Reactor) and ii) Separation of produced Vapor-Liquid
Fraction to pyro gases and liquid fuel with the help of a Cooler. The synergistic effect on the co-pyrolysis
of plastic and biomass blends is reported. Compared to pure polymer samples, the maximum
decomposition temperature of the mixture is also reduced from 4640C to 4500C. The Aspen HYSYS result
shows that bio-oil was the main product from pyrolysis at 4500C of the mixture. The final products of the
simulation are 82.29% bio-oil, 2.747% of gas, and, 14.96% char. It also showed that mixing the plastic
and biomass waste has a positive synergy on the quality and quantity of the produced bio-oil. The water
content of the bio-oil decreased from 26.87% to 13.27% when the ratio of plastic increased in the
mixture. The char content decreased from 35% to 14.96%. The developed simulation model can be a
bench mark for scale-up studies and will give an aspiration to the researchers for understanding the
actual product ranges. |
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