An Eulerian model for forest residues gasification in a plasma gasifier

被引:40
作者
Ismail, Tamer M. [1 ]
Monteiro, Eliseu [2 ,3 ]
Ramos, Ana [4 ]
Abd El-Salam, M. [5 ]
Rouboa, Abel [2 ,6 ,7 ]
机构
[1] Suez Canal Univ, Mech Engn Dept, Ismailia, Egypt
[2] Univ Porto, CIENER INEGI, Fac Engn, Porto, Portugal
[3] Polytech Inst Portalegre, VALORIZA Res Ctr Endogenous Resource Valorisat, Portalegre, Portugal
[4] Univ Porto, Fac Engn, INEGI FEUP, Porto, Portugal
[5] Cairo Univ, Dept Basic Sci, Giza, Egypt
[6] TAD Univ, Dept Engn, LAETA UTAD, Vila Real, Portugal
[7] Univ Penn, MEAM Dept, Philadelphia, PA 19020 USA
关键词
Plasma gasification model; Forest residues; CFD; Biomass; BUBBLING FLUIDIZED-BED; AIR-STEAM GASIFICATION; HYDROGEN-PRODUCTION; CO-GASIFICATION; BIOMASS; SIMULATION; GAS; PYROLYSIS; WASTE; CONVERSION;
D O I
10.1016/j.energy.2019.06.070
中图分类号
O414.1 [热力学];
学科分类号
摘要
A new mathematical model for plasma gasification was adopted and added to the COMMENT homemade code. The COMMENT code is dedicated to coupled transfer applications in the fields of thermal, fluid mechanics and chemical engineering, both solid and gaseous states being assessed. Phenomena like continuity, species transport, heat transfer, turbulence and chemical reactions were taken into account. Plasma gasification of forest residues was simulated within defined conditions and assumptions, the producer gas being monitored and characterized. The presented model was validated against literature data. A high level of agreement between the numerical and the experimental values was achieved, proving that the model is robust and suitable for the proposed goal. This new model requires low computational capacity and allows a wide range of reactor types to be used in the gasification process. A parametric study was also conducted in order to understand the influence of some variables on gasification products and their concentrations along the runs. It was possible to conclude that lower equivalence ratios (ER) favored H-2 and CO production as well as lower heating value (LHV), while higher ER values enhanced N-2 contents, carbon conversion efficiency (CCE) and minor alterations were observed for CH4 and CO2. H-2, N-2 and CO2 as well as CCE and cold-gas efficiency (CGE) were also enhanced by higher steam-to-biomass ratios (SBR), while CO content and LHV dropped, CH4 remaining almost unaltered. For higher temperatures H-2, CO and N-2 levels were improved as well as LHV, whereas CO2 and CGE were reduced and CH4 remained unchanged. The results showed that the model proposed in this study is a promising tool for simulating the plasma gasification process of biomass within a gasifier. (C) 2019 Elsevier Ltd. All rights reserved.
引用
收藏
页码:1069 / 1083
页数:15
相关论文
共 97 条
[1]   Fluidised bed co-gasification of coal and olive oil industry wastes [J].
André, RN ;
Pinto, F ;
Franco, C ;
Dias, M ;
Gulyurtlu, I ;
Matos, MAA ;
Cabrita, I .
FUEL, 2005, 84 (12-13) :1635-1644
[2]  
[Anonymous], 16 S INT COMB
[3]  
Antal M.J., 1985, Advances in solar energy, P175, DOI [10.1007/978-1-4613-9951-3_4, DOI 10.1007/978-1-4613-9951-3_4]
[4]   EFFECTS OF REACTOR SEVERITY ON THE GAS-PHASE PYROLYSIS OF CELULOSE-DERIVED AND KRAFT LIGNIN-DERIVED VOLATILE MATTER [J].
ANTAL, MJ .
INDUSTRIAL & ENGINEERING CHEMISTRY PRODUCT RESEARCH AND DEVELOPMENT, 1983, 22 (02) :366-375
[5]  
Antal MJ., 1985, Fundamentals of Thermochemical Biomass Conversion, P511
[6]   Numerical simulation and experimental analysis of gas/solid flow systems: 1999 Fluor-Daniel Plenary lecture [J].
Arastoopour, H .
POWDER TECHNOLOGY, 2001, 119 (2-3) :59-67
[7]  
Baudry C, 2004, P INT THERM SPRAY C
[8]  
Baudry C, 2003, P 16 ITN S PLASM CHE, P22
[9]   MASS AND OPTICAL-EMISSION SPECTROSCOPY OF PLASMAS FOR DIAMOND-SYNTHESIS [J].
BENNDORF, C ;
JOERIS, P ;
KROGER, R .
PURE AND APPLIED CHEMISTRY, 1994, 66 (06) :1195-1205
[10]   HETEROGENEOUS CRACKING OF WOOD PYROLYSIS TARS OVER FRESH WOOD CHAR SURFACES [J].
BOROSON, ML ;
HOWARD, JB ;
LONGWELL, JP ;
PETERS, WA .
ENERGY & FUELS, 1989, 3 (06) :735-740