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Reducing coke formation and extending lifetime of the HZSM-5 catalyst via co-pyrolysis of high density polyethylene with
switchgrass(Panicum virgatum)
Frankie Lazauskas, Drexel University, Department of Biodiversity, Earth, and Environmental Sciences
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Background: Pyrolysis
• Thermochemical decomposition of organic matter in the absence of oxygen which can produce solid, liquid, and gas products
• Biomass fast pyrolysis oil is a complex mixture of many oxygenated hydrocarbons and water (Acids, esters, ketones, aldehydes, sugars, furans, phenols, 15-30% water)
• Other issues with biomass pyrolysis oil include its high acidity, low heating value, thermal instability, and high oxygen/low hydrogen content(compared to petroleum oil)
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Background: Catalytic Fast Pyrolysis(CFP)
• Same as fast pyrolysis, except products pass over a reactive catalyst bed
• Often a zeolite catalyst, such as HZSM-5, that selectively makes deoxygenated aromatic hydrocarbons
• CFP of biomass creates coke while losing H, this coke formation eventually leads to deactivation of the catalyst
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Background: Agricultural Plastic Waste
• Many different plastics used for agricultural needs such as hay bale covers, pesticide/insecticide containers, transportation/storage of crops, etc.
• 521 million pounds of agricultural plastic waste every year in the U.S alone with about 70% being polyethylene
• Disposal Solutions
• Incineration, burial, and landfills come with many environmental concerns
• Simply recycling them can be difficult/expensive(toxins from pesticides)
• Co-pyrolysis feedstock
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Objective
• How does addition of HDPE affect product formation?
• Does addition of HDPE have an effect on coke formation and the lifetime of the catalyst?
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Materials & Methods
• CDS pyrolyzer(CDS Pyroprobe 5250-T) and external reactor(CDS 5250-TR)
• Agilent GC/MS(6890N)
• Quartz tube with ~1mg of sample(Switchgrass, HDPE, and 1:1 mixture) stuffed with quartz wool to prevent loss of sample
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Materials & Methods
• Pyrolysis done at 650°C with either 30 sample or 60 sample runs
• Gases transferred to external reactor and passed over HZSM-5 bed with ~15mg of catalyst at 500°C
• Products then analyzed by GC/MS
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Materials & Methods
• Spent catalyst with quartz wool removed post-run
• Quartz wool separated from spent catalyst
• Spent catalyst heated to 650°C, weight loss recorded for determining coke formation on HZSM-5
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Results: Coke Formation
1:1 Switchgrass HDPE
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Results: HZSM-5 Lifetime and Product Formation (Switchgrass Alone)
BTEX is the sum of the aromatic
compounds Benzene, Toluene,
Ethylbenzene, p-Xylene, and o-Xylene.
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Results: HZSM-5 Lifetime and Product Formation (HDPE Alone)
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Results: HZSM-5 Lifetime and Product Formation (1:1 Mix of HDPE and Switchgrass)
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Results: Deactivation of HZSM-5
• Production of acetic acid increased as more sample was run over HZSM-5 for all switchgrass runs
• No acetic acid detected in any of the HDPE runs
• Only 1 out of 4 of the mixed runs showed any acetic acid production(highest value ~12)
0 10 20 30 40 50 60 700
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10
15
20
25
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Acetic Acid for all SWG runs
SWG_A1-30SWG_B1-30SWG_C1-60SWG_D1-60
Amount of Sample Catalyst Exposed To(mg)
Are
a/M
ass(
mg)
/100
0000
0
Conclusions
• Addition of HDPE reduces coke formation which helps to delay deactivation of HZSM-5
• HDPE increased yield of stable aromatic hydrocarbons compared to biomass alone with a synergistic effect(1:1 ratio showed consistently higher yields)
Future Directions
• Understanding chemical pathways for the observed synergistic effect in mixed samples testing of other biomass/plastic combinations
• Different/smaller ratios of plastic to biomass, how much plastic is needed to still utilize this effects?
• Potential options for external reactor that is compatible with Shimadzu GC/MS models could mitigate many of the maintenance issues that hindered this project
Acknowledgements
Special thanks to
Dr. Akwesi Boateng, Dr. Charles Mullen, Tom Coleman and the entire pyrolysis team!
Questions?