Title of article
Co-pyrolysis of residual oil and polyethylene in sub- and supercritical water
Author/Authors
Bai، نويسنده , , Fan and Zhu، نويسنده , , Chun-Chun and Liu، نويسنده , , Yin and Yuan، نويسنده , , Pei-Qing and Cheng، نويسنده , , Zhen-Min and Yuan، نويسنده , , Wei-Kang، نويسنده ,
Issue Information
روزنامه با شماره پیاپی سال 2013
Pages
8
From page
267
To page
274
Abstract
At the temperature of 693 K and water densities from 0.10 to 0.30 g/cm3, co-pyrolysis of residual oil and polyethylene in sub- and supercritical water (sub-CW and SCW) was experimentally investigated. With the increase in water density, the phase structure of the co-pyrolysis system may evolve from a liquid/liquid/solid three-phase structure to a liquid/solid two-phase one. By co-pyrolysis of polyethylene with residual oil, H-rich paraffins, the main pyrolysis product of polyethylene, are released continuously into the reaction system. At higher water densities with the favorable liquid/solid two-phase structure, the contact of aromatic radicals from the pyrolysis of residual oil and paraffins from that of polyethylene is promoted, ensuring the coupling between pyrolysis networks of residual oil and polyethylene. Consequently, dealkylation of aromatic radicals may follow the desired mechanism by which the production of coke-inducing components is effectively depressed. A significantly reduced coke yield is observed in the co-pyrolysis of residual oil and polyethylene in sub-CW and SCW.
Keywords
Co-pyrolysis , supercritical water , Polyethylene , Residual oil
Journal title
Fuel Processing Technology
Serial Year
2013
Journal title
Fuel Processing Technology
Record number
1509448
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