In Situ and Ex Situ Catalytic Co-pyrolysis of Lignocellulosic Biomass and Plastics (Low-Density and High-Density Polyethylene) Using Spent FCC Catalyst

被引:7
作者
Kanduri, Praveen Kumar [1 ]
Seethamraju, Srinivas [1 ]
机构
[1] Indian Inst Technol, Dept Energy Sci & Engn, Mumbai 400076, Maharashtra, India
关键词
Pyrolysis; Spent FCC; Biomass; Plastics; In situ; Ex situ; GRADE BIO-OIL; AROMATICS; HYDRODEOXYGENATION; POLYPROPYLENE; CELLULOSE; HZSM-5;
D O I
10.1007/s12649-022-01961-0
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
Catalytic co-pyrolysis of biomass and plastics (low-density and high-density polyethylene) was conducted utilizing spent fluid-catalytic-cracking catalyst. The effect of pyrolysis type (in situ vs. ex situ) on product yield and selectivity was tested at feed ratios of 1:2, 1:1, and 2:1 (w/w). The ex situ configuration improved the bio-oil quality and produced substantially high gas and low char yields than the in situ configuration. The bio-oil from ex situ processes had more oxygen-free monoaromatics with a maximum yield of similar to 29%C and similar to 26%C for low-density and high-density polyethylene at the biomass to plastic ratios of 2 and 1, respectively. The feed containing more biomass resulted in a higher selectivity towards monoaromatics (including benzene, toluene, and xylene) and polycyclic aromatic hydrocarbons, regardless of the configuration type. Compared to biomass pyrolysis, co-feeding plastics with biomass enriched the hydrogen content of the bio-oil with the ex situ processes producing more fungible products than the in situ processes. The effective H/C ratio in the bio-oils improved from similar to 0.19 to > 1.0 for the biomass-plastic mixtures compared to biomass pyrolysis alone. This is so as the plastics are hydrogen rich (H/C ratio of 2) compared to biomass, and the increased hydrogen availability during pyrolysis reactions improves the biooil quality and simultaneously reduces the char formation. [GRAPHICS] .
引用
收藏
页码:1737 / 1751
页数:15
相关论文
共 43 条
[1]  
Agrio, about us
[2]  
[Anonymous], 2019, WORLD EN OUTL
[3]  
[Anonymous], OUTLOOK ENERGY PERSP
[4]  
[Anonymous], 2019, BP Energy Outlook
[5]   Production of green aromatics and olefins by catalytic fast pyrolysis of wood sawdust [J].
Carlson, Torren R. ;
Cheng, Yu-Ting ;
Jae, Jungho ;
Huber, George W. .
ENERGY & ENVIRONMENTAL SCIENCE, 2011, 4 (01) :145-161
[6]  
CHEN NY, 1988, ACS SYM SER, V376, P277
[7]   Catalytic fast pyrolysis of biomass to produce furfural using heterogeneous catalysts [J].
Chen, Xu ;
Yang, Haiping ;
Chen, Yingquan ;
Chen, Wei ;
Lei, Tingzhou ;
Zhang, Wennan ;
Chen, Hanping .
JOURNAL OF ANALYTICAL AND APPLIED PYROLYSIS, 2017, 127 :292-298
[8]   Minimization of Waste Spent Catalyst in Refineries [J].
Chiranjeevi, T. ;
Pragya, R. ;
Gupta, S. ;
Gokak, D. T. ;
Bhargava, S. .
WASTE MANAGEMENT FOR RESOURCE UTILISATION, 2016, 35 :610-617
[9]   Renewable aromatics through catalytic pyrolysis of coconut fiber (Cocos nucifera Linn.) using low cost HZSM-5 [J].
Costa, Juliana E. B. ;
Barbosa, Andrey S. ;
Melo, Marcus A. F. ;
Melo, Dulce M. A. ;
Medeiros, Rodolfo L. B. A. ;
Braga, Renata M. .
RENEWABLE ENERGY, 2022, 191 :439-446
[10]   Overview of applications of biomass fast pyrolysis oil [J].
Czernik, S ;
Bridgwater, AV .
ENERGY & FUELS, 2004, 18 (02) :590-598