Improving hydrocarbons production via catalytic co-pyrolysis of torrefied-biomass with plastics and dual catalytic pyrolysis
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Improving hydrocarbons production via catalytic co-pyrolysis of torrefied-biomass with plastics and dual catalytic pyrolysis
Improving hydrocarbons production via catalytic co-pyrolysis of torrefied-biomass with plastics and dual catalytic pyrolysis
中国化学工程学报(英文版)2022年42卷第2期 页码:196-209
Affiliations:
1. Key Laboratory of Thermal Energy Conversion and Control Ministry of Education, Southeast University,Nanjing,China,210096
2. Department of Mechanical Engineering, Juba University, Juba, P.O. Box 82, South Sudan
Author bio:
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DOI:
中图分类号:
纸质出版:2022
Accepted:
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Peter Keliona Wani Likun, Huiyan Zhang, Yuyang Fan. Improving hydrocarbons production via catalytic co-pyrolysis of torrefied-biomass with plastics and dual catalytic pyrolysis[J]. 中国化学工程学报(英文版), 2022,42(2):196-209.
catalytic co-pyrolysis of torrefied-biomass with plastics and dual catalytic pyrolysis[J]. 中国化学工程学报, 2022, 42(2): 196-209.
Peter Keliona Wani Likun, Huiyan Zhang, Yuyang Fan. Improving hydrocarbons production via catalytic co-pyrolysis of torrefied-biomass with plastics and dual catalytic pyrolysis[J]. 中国化学工程学报(英文版), 2022,42(2):196-209.DOI:
catalytic co-pyrolysis of torrefied-biomass with plastics and dual catalytic pyrolysis[J]. 中国化学工程学报, 2022, 42(2): 196-209.DOI:
Improving hydrocarbons production via catalytic co-pyrolysis of torrefied-biomass with plastics and dual catalytic pyrolysis
To increase the low yield and selectivity of aromatic hydrocarbons during the biomass pyrolysis process
we torrefied the biomass and then co-pyrolyzing with plastics such as high-density polyethylene (HDPE)
polystyrene (PS)
ethylene-vinyl acetate (EVA) and polypropylene (PP) and also single and dual catalyst layouts were investigated by Py-GC/MS. The results showed that non-catalytic fast pyrolysis (CFP) of raw bagasse (RBG) generated no aromatics. After torrefaction non-CFP of torrefied bagasse (TBG) generated low aromatic yield. Indicating that torrefaction would enhance the proportion of aromatics during the pyrolysis process. The CFP of TBG
200℃
and TBG
240℃
over ZSM-5 produced the total aromatic yield of 1.96 and 1.88 times higher
respectively
compared to non-CFP of TBG. Furthermore
the addition of plastic could increase H/Ceff ratio of the mixture
consequently
increase the yield of aromatic compounds. Among the various torrefied-bagasse/plastic mixtures
the CFP of TBG/EVA (7:3 ratio) mixture generated the highest the total aromatic yield of 7.7 times more than the CFP of TBG alone. The dual catalyst layout could enhance the yield of aromatics hydrocarbons. The dual-catalytic c
o-pyrolysis of TBG
200℃
/plastic (1:1) ratio over USY (ultra-stable Y zeolite)/ZSM-5
improved the total aromatics yield by 4.33 times more than the catalytic pyrolysis of TBG
200oC
alone over ZSM-5 catalyst. The above results showed that the yield and selectivities of light aromatic hydrocarbons can be improved
via
catalytic co-pyrolysis and dual catalytic co-pyrolysis of torrefied-biomass with plastics.
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