Influence of temperature and reaction time on the conversion of polystyrene waste to pyrolysis liquid oil
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- 作者：R. Miandada ; b ; A.S. Nizamib ; anizami@kau.edu.sa" class="auth_mail" title="E-mail the corresponding author ; nizami_pk@yahoo.com" class="auth_mail" title="E-mail the corresponding author ; M. Rehanb ; M.A. Barakata ; M.I. Khanc ; A. Mustafac ; I.M.I. Ismailb ; J.D. Murphyd ; e
- 关键词：CO ; carbon monoxide ; HDPE ; high density polyethylene ; HHV ; higher heating value ; KACARE ; King Abdullah City of Atomic and Renewable Energy ; KSA ; Kingdom of Saudi Arabia ; LDPE ; low density polyethylene ; MSW ; municipal solid waste ; NOx ; oxides of nitrogen ; PE ; polyethylene ; PP ; polypropylene ; PS ; polystyrene ; RDF ; refuse derived fuel ; SWM ; solid waste management ; TGA ; thermogravimetric analyzer ; TIC ; total ion chromatogram ; WTE ; waste-to-energy
- 刊名：Waste Management
- 出版年：2016
- 出版时间：December 2016
- 年：2016
- 卷：58
- 期：Complete
- 页码：250-259
- 全文大小：2148 K
文摘
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Polystyrene comprises 14.7% of municipal solid waste in Saudi Arabia.
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The optimum temperature for pyrolysis was 450 °C at 75 min retention time.
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At optimum conditions liquid fuel was 76% by mass of polystyrene.
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The liquid fuel had a high energy value of 41.2 GJ/t and density (0.92 g/cm3).
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The liquid fuel had low pour point (−18 °C) and freezing point (−64 °C).