Thermogravimetric pyrolysis of waste polyethylene-terephthalate and polystyrene: A critical assessment of kinetics modelling
Introduction
The total plastic consumption in Western Europe exceeded 52 million tonnes in 2008 (Baeyens et al., 2010). These plastics include mostly polyethylene (PE – 37 wt%), polypropylene (PP – 19 wt%), polyvinyl chloride (PVC – 19 %), polystyrene (PS – 6 %) and polyethylene terephthalate (PET – 6 wt%). Thermoplastics are widely applied in industrial and commercial products, and usually contain stabilisers and additives. Household solid waste (HSW) consists of 7–8 wt%, or up to 20 vol% of the post-consumer plastic solid waste (PSW) (Al-Salem et al., 2010, Baeyens et al., 2010).
Treatment and disposal of post-consumer plastics have become an important environmental concern, with recovery and recycling, landfilling and (co-)incineration as most applied methods. Incineration gains interest, due to increasing landfilling constraints and taxes, and due to the difficulties encountered when attempting to recycle mixed plastic wastes (Al-Salem et al., 2009a, Al-Salem et al., 2009b, Al-Salem et al., 2010). The research focus has recently shifted towards pyrolysis or gasification as thermal treatments. Whereas high temperature gasification targets the production of a syngas, to be further upgraded to fuel-grade organics or directly used in electricity generation, pyrolysis takes place in the absence of oxygen at moderate temperatures and recycles plastic solid waste (PSW) into chemicals and/or fuel: the polymer structure is decomposed into smaller intermediate products, usable as fuel or as raw materials for the petrochemical industry. By producing value-added products (such as liquid and gaseous fuel, polymer monomers and/or a carbonaceous residue as a candidate for possible upgrading to activated carbon or carbon black), pyrolysis can overcome certain disadvantages of incineration and recycling (Brems et al., 2011). The low temperature of the process and the absence of oxygen, moreover, reduce emission problems as encountered during incineration, where large volumes of combustion gas and toxic pollutants are produced (Everaert and Baeyens, 2002, Bhandare et al., 1997). Co-incineration is moreover controlled by stringent emission standards as e.g. set by the EU Hazardous Waste Incineration Directive (EU, 2000). It is difficult to treat or recycle mixed PSW, due to its complex nature and composition, the contamination with various residues (organic, inorganic or biological), and the possible structural deterioration of the polymeric compounds.
When pyrolysing PSW, only 5% of the energy content is used in the endothermic cracking process (Brems et al., 2011). Pyrolysis is therefore considered as one of the most promising methods to recover material and energy from PSW. Furthermore, almost all types of plastics (commingled or mixed with other materials such as wood, paper, ink, paint) can be treated. Pigments, inorganic fillers, supports and other additives, possibly present in minor concentrations in the polymers, are mostly retained in the solid residue.
Due to possible interactions during decomposition and interactions between the components of the mixture and the low molecular weight products and free radicals formed by the scission of the polymeric chains, thermal degradation of polymer mixtures gets more complex than degradation of single polymers (Williams and Williams, 1999). These interactions can affect the quality of the products formed and are hence important when high quality standards have to be met for use as feedstock or fuel (Al-Salem et al., 2009b, Al-Salem et al., 2010).
The objectives of the present research were twofold, i.e. (i) to study the experimental pyrolytic degradation of 2 important thermoplastics, PET and PS; and (ii) to critically assess the multiple model treatment methods proposed in literature to determine the Arrhenius-based kinetic parameters of the pyrolysis reaction as often experimentally determined by TGA. There is indeed some literature controversy concerning the applicability of simple TGA experiments to define the pyrolysis kinetics, with results widely different according to the conversion model applied. TGA experiments are, however, easy and fast and can provide correct kinetic values, comparable with isothermal results, if the correct data treatment is applied (Brems et al., 2011, Al-Salem et al., 2010). A study of isothermal pyrolysis of polyethylene is e.g. recently proposed by Al-Salem and Lettieri (2010).
Section snippets
Materials and methods
As stated before, the thermal behaviour of polymers is usually investigated by thermogravimetric analysis (TGA) and differential scanning calorimetry (DSC). These methods provide useful information on the thermal characteristics of materials, e.g. melting point, weight loss during thermal degradation, glass transition temperature, heat of crystallisation, etc. Based on these parameters, a kinetic model can be established to predict the reactor behaviour and a product distribution can be
Thermogravimetric degradation results of PET and PS
Fig. 1, Fig. 2 show the TGA and DTG curves of PET and PS, DTG being determined from the TGA as ΔMt/Δt versus T. The curves were obtained during the pyrolysis process under inert N2 atmosphere at different heating rates, β. The data obtained for temperatures below 350 and 300 °C are omitted in the figures, since the loss of weight recorded is minimum.
As seen from the figures, the pyrolysis stage is clearly defined between 380 and 470 °C for PET and 395–450 °C for PS respectively, and virtually
Comparison with literature data and data obtained in isothermal pyrolysis results
The present results for PET can be compared with both a previous literature survey, and dynamic or isothermal (fluidized bed) experiments as published by Brems et al. (2011): the isothermal activation energy was determined as 237 kJ/mol, whereas TGA experiments were modelled using the FWO-method to determine Ea for β = 100–120 K/min between 229 and 245 kJ/mol. These values in excess of 200 kJ/mol were also confirmed by Buyck (2007) and by Girija et al. (2005). Encinar and González (2008) observed
General conclusions
According to the model assessment, the concepts of a first or second order kinetics provide the most suitable design approach. A first order kinetics is commonly proposed in literature for a variety of plastics (Al-Salem et al., 2009a, Al-Salem et al., 2009b, Al-Salem and Lettieri, 2010, Brems et al., 2011). For both concepts, the activation energy is identical, since a function only of the plastic under scrutiny. The pre-exponential factor of the Arrhenius equation will however differ both in
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