Composition of products from the pyrolysis of polyethylene and polystyrene in a closed batch reactor: Effects of temperature and residence time

Abstract The compositions of the pyrolysis products of pure low-density polyethylene (LDPE) and polystyrene (PS) and their mixtures have been investigated over a temperature range from 300 to 500 °C. The pyrolysis experiments were carried out in a closed batch reactor under inert nitrogen atmosphere to study the effects of reaction temperature and residence time. LDPE was thermally degraded to oil at 425 °C however, beyond this temperature the proportion of oil product decreased as a result of its conversion to char and hydrocarbon gas. Compositional analysis of the oil products showed that aliphatic hydrocarbons were the major components, but the proportion of aromatic compounds increased at higher temperatures and residence times. On the other hand, PS degraded at around 350 °C, mainly into a viscous dark-coloured oil. The formation of char only increased marginally until 425 °C, but was dramatically enhanced at 450 and 500 °C, reaching up to 30 wt.%. The oil product from PS even at 350 °C consisted almost entirely of aromatic compounds especially toluene, ethylbenzene and styrene. Under increasing temperatures and residence times, the oil product from PS was preferentially converted to char, while gas formation was preferred for the oil from LDPE. For instance at 500 °C, PS produced about twice the amount of char obtained from LDPE indicating the role of aromatic compounds in char formation via condensation of the aromatic ring structure. During the co-pyrolysis of a 7:3 mixture of LDPE and PS, wax product was observed at 350 °C leading to oil at 400 °C, indicating that the presence of PS influenced the conversion of LDPE by lowering its degradation temperature. The mixture produced more oil and less char than the individual plastics at 450 °C.

[1]  Paul T. Williams,et al.  Hydrocarbon gases and oils from the recycling of polystyrene waste by catalytic pyrolysis , 2004 .

[2]  Robert L. White,et al.  Polyethylene catalytic hydrocracking by PtHZSM-5, PtHY, and PtHMCM-41 , 2004 .

[3]  Paul T. Williams,et al.  Fluidised bed pyrolysis of low density polyethylene to produce petrochemical feedstock , 1999 .

[4]  Isabel Cabrita,et al.  Pyrolysis of plastic wastes , 1999 .

[5]  Jingcui Liang,et al.  Thermal and catalytic degradation of high density polyethylene and commingled post-consumer plastic waste , 1997 .

[6]  J. Kuipers,et al.  Recycling of polyethene and polypropene in a novel bench-scale rotating cone reactor by high temperature pyrolysis. , 1998 .

[7]  P. Magnoux,et al.  Organic chemistry of coke formation , 2001 .

[8]  Paul T. Williams,et al.  Composition of oils derived from the batch pyrolysis of tyres , 1998 .

[9]  R. Lattimer Pyrolysis field ionization mass spectrometry of polyolefins , 1995 .

[10]  P. Williams,et al.  Analysis of products from the pyrolysis and liquefaction of single plastics and waste plastic mixtures , 2007 .

[11]  A. Lappas,et al.  Chemical recycling of plastic wastes made from polyethylene (LDPE and HDPE) and polypropylene (PP). , 2007, Journal of hazardous materials.

[12]  A. Marcilla,et al.  Evolution of products during the degradation of polyethylene in a batch reactor , 2009 .

[13]  D. Serrano,et al.  Conversion of low density polyethylene into petrochemical feedstocks using a continuous screw kiln reactor , 2001 .

[14]  L. Tiikma,et al.  Coprocessing of heavy shale oil with polyethylene waste , 2007 .

[15]  Don W. Green,et al.  Perry's Chemical Engineers' Handbook , 2007 .

[16]  G. Lopez,et al.  Product distribution modelling in the thermal pyrolysis of high density polyethylene. , 2007, Journal of hazardous materials.

[17]  J. Kuipers,et al.  Experimental Determination of the Yield of Pyrolysis Products of Polyethene and Polypropene. Influence of Reaction Conditions , 1998 .

[18]  I. Marco,et al.  Recycling polymeric wastes by means of pyrolysis , 2002 .

[19]  J. Scheirs,et al.  Feedstock recycling and pyrolysis of waste plastics , 2006 .

[20]  Roberto Aguado,et al.  Kinetics of polystyrene pyrolysis in a conical spouted bed reactor , 2003 .

[21]  Stefan Czernik,et al.  Fast pyrolysis of plastic wastes , 1990 .

[22]  A. Marcilla,et al.  Catalytic pyrolysis of LDPE over H-beta and HZSM-5 zeolites in dynamic conditions: Study of the evolution of the process , 2007 .

[23]  S. M. Sadrameli,et al.  Analytical representations of experimental polyethylene pyrolysis yields , 2004 .

[24]  Antonio Marcilla,et al.  Thermal Degradation of LDPE−Vacuum Gas Oil Mixtures for Plastic Wastes Valorization , 2007 .

[25]  W. Kaminsky,et al.  Feedstock recycling of polymers by pyrolysis in a fluidised bed , 2004 .

[26]  G. Lopez,et al.  Influence of FCC catalyst steaming on HDPE pyrolysis product distribution , 2009 .

[27]  W. Kaminsky,et al.  Catalytical and thermal pyrolysis of polyolefins , 2007 .

[28]  Jasmin Shah,et al.  Catalytic pyrolysis of low-density polyethylene with lead sulfide into fuel oil , 2005 .

[29]  P. Carniti,et al.  POLYSTYRENE THERMODEGRADATION .2. KINETICS OF FORMATION OF VOLATILE PRODUCTS , 1991 .

[30]  Paul T. Williams,et al.  Analysis of products derived from the fast pyrolysis of plastic waste , 1997 .