Full Length ArticleFuel production from pyrolysis of natural and synthetic rubbers
Introduction
Waste management is a global issue which impacts the sustainability of environmental and economic developments. Rubber waste in the forms of tyres, gloves or others have been a problematic material for treatment as it is highly resistant to bio-degradation. Natural rubber (NR) consists of an elastic polymer (cis-1, 4 polyisoprene) from latex which is almost all from the rubber tree (Hevea brasiliensis). Due to the shortage of natural rubber and purpose of various applications, currently the majority of the rubber market share is held by vulcanized synthetic rubber (SR) which is generally comprised of cross-linked long-chain man-made polymers (e.g., tyrene/butadiene and isobutylene/isoprene) with sulphur atoms. These artificial polymers are synthesised from fossil petroleum and then primarily used to make tyres. For instance, cis-polybutadiene rubber (CBR), isobutylene–isoprene copolymer rubber (i.e., butyl rubber, abbr. BR) and styrene–butadiene copolymer rubber (SBR) are three of the most common synthetic rubbers used in tyre manufacturing. A tyre may contain synthetic rubber, natural rubber, carbon black, steel, fabric, plasticizers, lubricants, antioxidants, antiozonants, inorganic materials (e.g., calcium carbonate and silica), and other components.
As the most abundant rubber waste, approximately 4 × 109 end-of-life tyres (equivalent to 3.2 × 108 tonnes) are estimated to be disposed through landfills and stockpiles worldwide [1]. In Australia, an annual estimate of more than 2 × 105 tonnes of waste tyres are landfilled or stockpiled [2].
According to the hierarchy of sustainable waste management by US EPA, the priority decreases in the order: source reduction and reuse > recycling and composting > energy recovery > treatment and disposal [3]. Considering the difficulties for the reuse or recycling of rubber wastes, energy and fuel generation through several thermo-chemical conversion technologies is gaining increased interest. In the EU, incineration for production of heat and/or electricity is the most common treatment technology followed by reuse and export [4]. Additional advanced technologies have been applied to recover fuels or chemicals from rubber wastes, such as gasification [5] and pyrolysis [6].
Pyrolysis technology thermally decomposes rubber or other organic wastes (e.g., biomass), in an inert atmosphere at temperatures of around 350–550 °C or higher, to give fuel products containing liquid pyrolysis oil, solid char and pyrolytic gas. The resulting products can be further and selectively upgraded into value-added fuels or chemicals [7], [8], [9], [10]. Many studies have been conducted on the pyrolysis of rubber materials. Choi [11] applied pyrolysis-GC to study the volatile pyrolysis products from 15 patterns of SBRs with different microstructures. It was found that butadiene, 4-vinylcyclohexene and styrene are the dominant products with the ratios affected by relative contents of styrene, 1,2, cis-1,4-, and trans-1,4-units. Danon et al. [12] identified the primary pyrolysis products of monomers and dimers from three different rubbers of NR, CBR and SBR using the instrument of combined thermogravimetric analyser and mass spectrometer (TGA-MS). However, in their research, the heat changes of the rubbers during pyrolysis, including specific and latent heats, and the properties of other products were not characterised. Lah et al. [13] modelled the pyrolysis kinetics of different tyre components of NR, BR, SBR and other fabric, oil and additives in scrap tyre rubber using a thermogravimetric analyser. Miranda et al. [14] also investigated the kinetics of waste tyre mainly consisting of NR, BR and SBR and determined the effect of temperature on the composition of pyrolysis oil products. It was observed that the lower temperature (<390 °C) favoured the formation of alkene products while the higher temperature favoured formation of aromatics. Williams [15] compared the waste tyre pyrolysis in various reactor types, such as fixed bed, moving screw bed, rotary kiln, vacuum, conical spouted bed, fluidised bed and drop tube reactor, and the oil, char and gas yields fell in the ranges of 5–63%, 22–49% and 3–73%, respectively.
The previous studies were mainly focused on the pyrolysis kinetics modelling of major components in lump waste tyres, characterisation of products (especially pyrolysis oil) from pyrolysis of a lump rubber tyre, or pyrolysis of NR products (e.g., latex gloves) [16], [17]. Few studies have been performed on the comprehensive comparison on the pyrolysis characteristics and differences between NR tyres and mats, and between NR and SR tyres. In this work, rubber materials from different resources including three tyre types (i.e., NR tyre, pneumatic tyre and SR tyre) and one NR mat, were subjected to slow pyrolysis process wherein the product properties were characterised. Mass and heat changes of the selected rubber materials were also investigated. The work will facilitate further understanding of pyrolysis of different rubber materials to generate fuels, which is beneficial in meeting the increasing global fuel demand.
Section snippets
Feedstock
All black rubber materials in the original forms were purchased from the distributor of J Blackwood & Son Pty Limited (Australia), including natural rubber tyre F50 coupling (abbr. NR–Tyre), natural rubber mat of 1200 mm × 1.59 mm (abbr. NR–Mat), pneumatic black rubber tyre (abbr. PR–Tyre, supplier: EHI Australia PTY LTD) and synthetic rubber tyre FRAS (fire resistant & anti-static) F40 (abbr. SR–Tyre). Rubber pieces were shredded from the tyres/mat and then ground with the assistance of liquid
Pyrolytic gas
The evolution rates of the major gas components including H2, CO2, CO, CH4, C2H4, and C2H6 during pyrolysis of different rubbers are depicted in Fig. 1. The overall gas yield (wt.% of raw rubber feed, in black broken line) versus temperature was obtained by integrating the total evolution rate of all gases with temperature.
For NR–Tyre, the CO2 evolution rate formed a wide but low hump at around 225–450 °C. Between 350 and 525 °C, H2 was the dominant gas species, shaping a double-peak curve with a
Conclusion
In this study, four different rubber samples including natural rubber tyre, pneumatic tyre, synthetic rubber tyre and one natural rubber mat were pyrolysed at 10 °C/min to generate fuel products of pyrolytic gas, pyrolysis oil and char. H2 and CO were basically the primary gas species in the gas product, indicating the potential of using the pyrolytic gas for syngas or hydrogen production. Compared to NR–Tyre, NR–Mat had similar CO evolution but much lower H2 release. More obvious H2 generation
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