2007Ranliao huaxue xuebaoRequires access

Thermal behavior and dynamics of biomass and waste tyre co-pyrolysis oil

Qing Cao

Open publisher page 0 citations

Abstract

Thermal behaviors of commercial diesel oil 0# and pyrolysis oil obtained from co-pyrolysis of biomass and waste tyre blend(with or without catalysts) were investigated by thermogravimetric analysis(TG-DTG).Through linear regression,the results illustrated that for pyrolysis oils the thermal kinetic follows the formula dα/dt=Ae-△vapH/RT(1-α)2and for diesel oil it follows the formula dα/dt=1.5Ae-△vapH/RT(1α)2/3[1-(1-α)1/3]-1.The evaporation heats calculated were 37.46 kJ·mol-1 for SBA-catalyzed pyrolysis oil,30.60 kJ·mol-1 for MCM-41-catalyzed pyrolysis oil,41.27 kJ·mol-1 for pyrolysis oil without using any catalyst, and 55.50 kJ·mol-1 for diesel oil 0#;these values were close to those reported in the literature.The existence of SBA-15 and MCM-41 as catalysts in the pyrolysis can reduce high fractions of the resultant pyrolysis oil;SBA-15 performed better than MCM-41 in reducing high fractions.

About this research paper

What this paper is about

Thermal behaviors of commercial diesel oil 0# and pyrolysis oil obtained from co-pyrolysis of biomass and waste tyre blend(with or without catalysts) were investigated by thermogravimetric analysis(TG-DTG).Through linear regression,the results illustrated that for pyrolysis oils the thermal kinetic follows the formula dα/dt=Ae-△vapH/RT(1-α)2and for diesel oil it follows the formula dα/dt=1.5Ae-△vapH/RT(1α)2/3[1-(1-α)1/3]-1.The evaporation heats calculated were 37.46 kJ·mol-1 for SBA-catalyzed pyrolysis oil,30.60 kJ·mol-1 for MCM-41-catalyzed pyrolysis oil,41.27 kJ·mol-1 for pyrolysis oil without using any catalyst, and 55.50 kJ·mol-1 for diesel oil 0#;these values were close to those reported in the literature.The existence of SBA-15 and MCM-41 as catalysts in the pyrolysis can reduce high fractions of the resultant pyrolysis oil;SBA-15 performed better than MCM-41 in reducing high fractions.

Why it matters

A significance statement is not available in the OpenAlex record.

Key contribution

A contribution statement is not available in the OpenAlex record.

Method / approach

Method details are not available in the OpenAlex metadata.

Main findings

Findings are not separately available in the OpenAlex metadata.

Limitations

Limitations are not available in the OpenAlex metadata.

Applications

Application details are not available in the OpenAlex metadata.

Available abstract

Thermal behaviors of commercial diesel oil 0# and pyrolysis oil obtained from co-pyrolysis of biomass and waste tyre blend(with or without catalysts) were investigated by thermogravimetric analysis(TG-DTG).Through linear regression,the results illustrated that for pyrolysis oils the thermal kinetic follows the formula dα/dt=Ae-△vapH/RT(1-α)2and for diesel oil it follows the formula dα/dt=1.5Ae-△vapH/RT(1α)2/3[1-(1-α)1/3]-1.The evaporation heats calculated were 37.46 kJ·mol-1 for SBA-catalyzed pyrolysis oil,30.60 kJ·mol-1 for MCM-41-catalyzed pyrolysis oil,41.27 kJ·mol-1 for pyrolysis oil without using any catalyst, and 55.50 kJ·mol-1 for diesel oil 0#;these values were close to those reported in the literature.The existence of SBA-15 and MCM-41 as catalysts in the pyrolysis can reduce high fractions of the resultant pyrolysis oil;SBA-15 performed better than MCM-41 in reducing high fractions.

Key concepts: Pyrolysis, Pyrolysis oil, Chemistry, Thermogravimetric analysis, Diesel fuel, Catalysis, Biomass (ecology), Chemical engineering

Related papers

Back to paper searchBrowse research topicsOriginal source
Thermal behavior and dynamics of biomass and waste tyre co-pyrolysis oil — Research Paper | ScholarLens