Pyrolysis-catalytic dry (CO2) reforming of waste plastics for syngas production: Influence of process parameters

被引:46
作者
Saad, Juniza Md [1 ,2 ]
Williams, Paul T. [1 ]
机构
[1] Univ Leeds, Sch Chem & Proc Engn, Leeds LS2 9JT, W Yorkshire, England
[2] Univ Tenaga Nas, Jalan IKRAM UNITEN, Selangor, Malaysia
关键词
Waste; Plastics; Reforming; Carbon dioxide; Catalyst; HYDROGEN-PRODUCTION; SYNTHESIS GAS; METHANE; TEMPERATURE; REACTOR;
D O I
10.1016/j.fuel.2016.12.014
中图分类号
TE [石油、天然气工业]; TK [能源与动力工程];
学科分类号
0807 ; 0820 ;
摘要
Catalytic dry (CO2) reforming of waste plastics was carried out in a two stage, pyrolysis-catalytic reforming fixed bed reactor to optimise the production of syngas (H-2 + CO). The effects of changing the process parameters of, catalyst preparation conditions, catalyst temperature, CO2 input rate and catalyst:plastic ratio were investigated. The plastics used was a mixture of plastics simulating that found in municipal solid waste and the catalyst used was Ni-Co-Al2O3. The results showed that changing each of the process conditions investigated, all significantly influenced syngas production. An increase of 17% of syngas production was achieved from the experiment with the catalyst prepared by rising-pH technique compared to preparation via the impregnation method. The optimum syngas production of 148.6 mmol(syngas) g(swp)(-1) was attained at the catalytic dry reforming temperature of 800 degrees C and catalyst:plastic ratio of 0.5. The increase of CO2 input rate promoted a higher yield of syngas. (C) 2016 Elsevier Ltd. All rights reserved.
引用
收藏
页码:7 / 14
页数:8
相关论文
共 28 条
[1]   Sono-synthesis and characterization of bimetallic Ni-Co/Al2O3-MgO nanocatalyst: Effects of metal content on catalytic properties and activity for hydrogen production via CO2 reforming of CH4 [J].
Abdollahifar, Mozaffar ;
Haghighi, Mohammad ;
Babaluo, Ali Akbar ;
Talkhoncheh, Saeed Khajeh .
ULTRASONICS SONOCHEMISTRY, 2016, 31 :173-183
[2]  
Aguado J., 1999, FEEDSTOCK RECYCLING
[3]   Comparison of dry reforming of methane in low temperature hybrid plasma-catalytic corona with thermal catalytic reactor over Ni/γ-Al2O3 [J].
Aziznia, Amin ;
Bozorgzadeh, Hamid Reza ;
Seyed-Matin, Naser ;
Baghalha, Morteza ;
Mohamadalizadeh, Ali .
JOURNAL OF NATURAL GAS CHEMISTRY, 2012, 21 (04) :466-475
[4]   Modelling of methane dry reforming over Ni/Al2O3 catalyst in a fixed-bed catalytic reactor [J].
Benguerba, Yacine ;
Dehimi, Lila ;
Virginie, Mirella ;
Dumas, Christine ;
Ernst, Barbara .
REACTION KINETICS MECHANISMS AND CATALYSIS, 2015, 114 (01) :109-119
[5]   Catalytic steam reforming of model compounds of biomass pyrolysis liquids in fixed bed: Acetol and n-butanol [J].
Bimbela, F. ;
Oliva, M. ;
Ruiz, J. ;
Garcia, L. ;
Arauzo, J. .
JOURNAL OF ANALYTICAL AND APPLIED PYROLYSIS, 2009, 85 (1-2) :204-213
[6]  
Bustamante F., 2002, Fuel Chem. Div, V47, P663
[7]  
de Adrados A, 2012, WASTE MANAGE, V32, P826
[8]  
Delgado C, 2007, JRC37456
[9]   Dry Reforming of Methane - Review of Feasibility Studies [J].
Er-rbib, Hanaa ;
Bouallou, Chakib ;
Werkoff, Francois .
PRES 2012: 15TH INTERNATIONAL CONFERENCE ON PROCESS INTEGRATION, MODELLING AND OPTIMISATION FOR ENERGY SAVING AND POLLUTION REDUCTION, 2012, 29 :163-168
[10]   Plastic waste as a fuel - CO2-neutral or not? [J].
Eriksson, Ola ;
Finnveden, Goran .
ENERGY & ENVIRONMENTAL SCIENCE, 2009, 2 (09) :907-914