Supercritical water gasification of biomass and agro-food residues: Energy assessment from modelling approach

被引:42
作者
Macri, Domenico [1 ,4 ]
Catizzone, Enrico [2 ]
Molino, Antonio [3 ]
Migliori, Massimo [1 ]
机构
[1] Univ Calabria, Dept Environm & Chem Engn, Via P Bucci Cubo 42a, I-87036 Arcavacata Di Rende, CS, Italy
[2] Italian Natl Agcy New Technol Energy & Sustainabl, Trisaia Res Ctr, ENEA, I-75026 Rotondela, MT, Italy
[3] Italian Natl Agcy New Technol Energy & Sustainabl, Res Ctr Partici, ENEA, Piazzale Enrico Fermi 1, Portici, NA, Italy
[4] UCL, Dept Chem Engn, London WC1E 7JE, England
关键词
Supercritical water gasification; Thermodynamic modelling; Waste-to-Hydrogen; Energy process integration; HYDROGEN-PRODUCTION; THERMODYNAMIC ANALYSIS; HYDROTHERMAL GASIFICATION; GLUCOSE GASIFICATION; SYNGAS PRODUCTION; GREEN CHEMICALS; HYBRID SYSTEMS; SEWAGE-SLUDGE; MICROALGAE; CELLULOSE;
D O I
10.1016/j.renene.2019.12.147
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
The gasification of biomass in supercritical water is a promising technology for hydrogen production and the paper reports a thermodynamic analysis, based on minimization of Gibbs free energy, of the gasification with supercritical water of different biomass and agro-food residues: almond shells, digestate from wastewater treatment, algae and manure sludge. Numerical simulations were performed in order to assess the effect of temperature, pressure and biomass-to-water ratio on gas-phase yield and composition. A partial energy integration was also discussed, by considering the energy recovery from a turbine expansion of the gas-phase stream leaving the gasifier. The proposed thermodynamic approach allows predicting not only gasification efficiency of gasifier but also energy balance on the entire gasification process. Results showed that the dry substrates (almond shells and algae more than digestate and sludge) tend to form more carbon monoxide. Besides, data comparison revealed that the produced hydrogen comes from biomass and water for high process temperature, while when temperature decreases, the thermodynamic path tends to promote water formation from the hydrogen of the dry biomass. (C) 2020 Elsevier Ltd. All rights reserved.
引用
收藏
页码:624 / 636
页数:13
相关论文
共 46 条
[1]   Biomass gasification in supercritical water [J].
Antal, MJ ;
Allen, SG ;
Schulman, D ;
Xu, XD ;
Divilio, RJ .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2000, 39 (11) :4040-4053
[2]   Catalytic features of CuZnZr-zeolite hybrid systems for the direct CO2-to-DME hydrogenation reaction [J].
Bonura, G. ;
Frusteri, F. ;
Cannilla, C. ;
Ferrante, G. Drago ;
Aloise, A. ;
Catizzone, E. ;
Migliori, M. ;
Giordano, G. .
CATALYSIS TODAY, 2016, 277 :48-54
[3]   Hydrogen production from supercritical water gasification of chicken manure [J].
Cao, Wen ;
Cao, Changqing ;
Guo, Liejin ;
Jin, Hui ;
Dargusch, Matthew ;
Bernhardt, Debra ;
Yao, Xiangdong .
INTERNATIONAL JOURNAL OF HYDROGEN ENERGY, 2016, 41 (48) :22722-22731
[4]   Supercritical water gasification: a patents review [J].
Casademont, Pau ;
Belen Garcia-Jarana, M. ;
Sanchez-Oneto, Jezabel ;
Ramon Portela, Juan ;
Martinez de la Ossa, Enrique J. .
REVIEWS IN CHEMICAL ENGINEERING, 2017, 33 (03) :237-261
[5]   Supercritical water gasification of biomass: Thermodynamic constraints [J].
Castello, Daniele ;
Fiori, Luca .
BIORESOURCE TECHNOLOGY, 2011, 102 (16) :7574-7582
[6]   Towards Solar Fuels from Water and CO2 [J].
Centi, Gabriele ;
Perathoner, Siglinda .
CHEMSUSCHEM, 2010, 3 (02) :195-208
[7]   Catalytic and Non-catalytic Supercritical Water Gasification of Microalgae and Glycerol [J].
Chakinala, Anand G. ;
Brilman, Derk W. F. ;
van Swaaij, Wim P. M. ;
Kersten, Sascha R. A. .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2010, 49 (03) :1113-1122
[8]   A comparison of gasification phenomena among raw biomass, torrefied biomass and coal in an entrained-flow reactor [J].
Chen, Wei-Hsin ;
Chen, Chih-Jung ;
Hung, Chen-I ;
Shen, Cheng-Hsien ;
Hsu, Heng-Wen .
APPLIED ENERGY, 2013, 112 :421-430
[9]   Hydrogen production by sewage sludge gasification in supercritical water with a fluidized bed reactor [J].
Chen, Yunan ;
Guo, Liejin ;
Cao, Wen ;
Jin, Hui ;
Guo, Simao ;
Zhang, Ximin .
INTERNATIONAL JOURNAL OF HYDROGEN ENERGY, 2013, 38 (29) :12991-12999
[10]   Thermodynamic analysis of hydrogen production from biomass gasification [J].
Cohce, M. K. ;
Dincer, I. ;
Rosen, M. A. .
INTERNATIONAL JOURNAL OF HYDROGEN ENERGY, 2010, 35 (10) :4970-4980