Published May 2012 | Version v1
Journal article

Pyrolysis of polyolefins for increasing the yield of monomers' recovery

  • 1. Royal Institute of Technology, School of Industrial Engineering and Management, Division of Energy and Furnace Technology, Brinellvagen 23, 100-44 Stockholm (Sweden)
  • 2. University of Hamburg, Institute of Technical and Macromolecular Chemistry, Martin-Luther-King Platz 6, 20146 Hamburg (Germany)
  • 3. State University of Campinas – UNICAMP, College of Chemical Engineering, Department of Polymer Science – Av. Albert Einstein 13083-852 Campinas (Brazil)

Description

Highlights: ► Thermal and catalytic pyrolysis of mixed polyolefins in fluidized bed has been studied. ► We tested applicability of a commercial Ziegler–Natta catalyst (Z–N: TiCl4/MgCl2). ► The catalyst has a strong influence on product distribution, increasing gas fraction. ► At 650 °C the monomer generation increased by 55% when the catalyst was used. ► We showed the concept of treatment of mixed polyolefins without a need of separation. - Abstract: Pyrolysis of plastic waste is an alternative way of plastic recovery and could be a potential solution for the increasing stream of solid waste. The objective of this work was to increase the yield the gaseous olefins (monomers) as feedstock for polymerization process and to test the applicability of a commercial Ziegler–Natta (Z–N): TiCl4/MgCl2 for cracking a mixture of polyolefins consisted of 46% wt. of low density polyethylene (LDPE), 30% wt. of high density polyethylene (HDPE) and 24% wt. of polypropylene (PP). Two sets of experiments have been carried out at 500 and 650 °C via catalytic pyrolysis (1% of Z–N catalyst) and at 650 and 730 °C via only-thermal pyrolysis. These experiments have been conducted in a lab-scale, fluidized quartz-bed reactor of a capacity of 1–3 kg/h at Hamburg University. The results revealed a strong influence of temperature and presence of catalyst on the product distribution. The ratios of gas/liquid/solid mass fractions via thermal pyrolysis were: 36.9/48.4/15.7% wt. and 42.4/44.7/13.9% wt. at 650 and 730 °C while via catalytic pyrolysis were: 6.5/89.0/4.5% wt. and 54.3/41.9/3.8% wt. at 500 and 650 °C, respectively. At 650 °C the monomer generation increased by 55% up to 23.6% wt. of total pyrolysis products distribution while the catalyst was added. Obtained yields of olefins were compared with the naphtha steam cracking process and other potentially attractive processes for feedstock generation. The concept of closed cycle material flow for polyolefins has been discussed, showing the potential benefits of feedstock recycling in a plastic waste management.

Availability note (English)

Available from http://dx.doi.org/10.1016/j.wasman.2011.10.009

Additional details

Identifiers

DOI
10.1016/j.wasman.2011.10.009;
PII
S0956-053X(11)00468-5;

Publishing Information

Journal Title
Waste Management
Journal Volume
32
Journal Issue
5
Journal Page Range
p. 840-846
ISSN
0956-053X
CODEN
WAMAE2

Optional Information

Copyright
Copyright (c) 2011 Elsevier Science B.V., Amsterdam, The Netherlands, All rights reserved.