Solar gasification of grape marc for syngas production: Solar-dish-coupled reactor basic engineering and optimization

被引:4
作者
Butti, Juan Manuel Leiva [1 ,2 ]
Mc Leod, Jorge E. Nunez [1 ,2 ]
Rivera, Selva S. [1 ]
机构
[1] Univ Nacl Cuyo, Fac Ingn, Inst CEDIAC, RA-5500 Mendoza, Argentina
[2] Univ Nacl Cuyo, Fac Ingn, CONICET, RA-5500 Mendoza, Argentina
关键词
Biomass gasification; Solar thermal power; Grape marc; Reactor design; Syngas; Waste to energy; OF-THE-ART; BIOMASS GASIFICATION; STEAM-GASIFICATION; DRIVEN GASIFICATION; CO-GASIFICATION; FLUIDIZED-BED; WOOD BIOMASS; DESIGN; FEEDSTOCK; TECHNOLOGIES;
D O I
10.1016/j.cep.2020.108050
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
In this paper, a new 5.8 kW solar biomass gasification reactor design is proposed. It is meant for energetic exploitation of grape marc, a residue of the wine-making industry. The design couples the reactor with a 3.0 m diameter Parabolic Dish Solar Concentrator, and contemplates controlling its temperature by manipulating the biomass inlet rate. This work aims to establish an upper limit on the reactor syngas yield under actual solar and environmental conditions, to determine the optimal dimensions of the reactor, and to evaluate the feasibility of the temperature control system. Also, a process is proposed for industrial application and practical implications are considered. The performance of the reactor was numerically simulated employing 1-min solar irradiance data, heat transfer models, reaction models and enthalpy balances. The reactor dimensions that maximize syngas production were determined. Simulation results showed an upper limit of 73 g(dry bass)/min for the grape marc inlet rate (stationary regime), and of 3180 Nm(3) (36.68 GJ) for the total syngas yield on the grape marc production season. Solar irradiance peaks were compensated, which supports the proposed temperature control system. Several design aspects were found to have substantial impact on the reactor performance, which contributes towards prototype manufacturing.
引用
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页数:17
相关论文
共 57 条
[1]   Kinetics of woodchips char gasification with steam and carbon dioxide [J].
Ahmed, I. I. ;
Gupta, A. K. .
APPLIED ENERGY, 2011, 88 (05) :1613-1619
[2]  
[Anonymous], 2015, Thermal radiation heat transfer, DOI DOI 10.1201/B18835
[3]  
[Anonymous], **DATA OBJECT**, DOI DOI 10.17632/JWXG2PC5ZD.1
[4]  
Basu P, 2010, BIOMASS GASIFICATION AND PYROLYSIS: PRACTICAL DESIGN AND THEORY, P1
[5]   Design, simulation and experimental study of a directly-irradiated solar chemical reactor for hydrogen and syngas production from continuous solar-driven wood biomass gasification [J].
Bellouard, Quentin ;
Rodat, Sylvain ;
Abanades, Stephane ;
Ravel, Serge ;
Frayssines, Pierre-Eric .
INTERNATIONAL JOURNAL OF HYDROGEN ENERGY, 2019, 44 (35) :19193-19205
[6]   Biomass Gasification in an Innovative Spouted-Bed Solar Reactor: Experimental Proof of Concept and Parametric Study [J].
Bellouard, Quentin ;
Abanades, Stephane ;
Rodat, Sylvain .
ENERGY & FUELS, 2017, 31 (10) :10933-10945
[7]  
Cengel Y.A., 2007, McGraw-Hill Series in Mechanical Engineering, V3rd, P227
[8]   Comprehensive performance assessment of a continuous solar-driven biomass gasifier [J].
Chuayboon, Srirat ;
Abanades, Stephan ;
Rodat, Sylvain .
FUEL PROCESSING TECHNOLOGY, 2018, 182 :1-14
[9]   Insights into the influence of biomass feedstock type, particle size and feeding rate on thermochemical performances of a continuous solar gasification reactor [J].
Chuayboon, Srirat ;
Abanades, Stephane ;
Rodat, Sylvain .
RENEWABLE ENERGY, 2019, 130 :360-370
[10]   Experimental analysis of continuous steam gasification of wood biomass for syngas production in a high-temperature particle-fed solar reactor [J].
Chuayboon, Srirat ;
Abanades, Stephane ;
Rodat, Sylvain .
CHEMICAL ENGINEERING AND PROCESSING-PROCESS INTENSIFICATION, 2018, 125 :253-265