The Gibbs Free Energy Gradient Method for RDF gasification modelling

被引:42
作者
Barba, D. [4 ]
Prisciandaro, M. [1 ]
Salladini, A. [2 ]
di Celso, G. Mazziotti [3 ]
机构
[1] Univ Aquila, Dept Chem Chem Engn & Mat, I-67100 Laquila, Italy
[2] Proc Innovat, I-67100 Laquila, Italy
[3] Univ Teramo, Dept Food Sci, I-64023 Mosciano Sant Angelo, Teramo, Italy
[4] Univ Campus Biomed Rome, I-00128 Rome, Italy
关键词
RDF; Gasification; Model; Equilibrium; Free energy; CIRCULATING FLUIDIZED-BED; BIOMASS GASIFICATION; COAL GASIFIER; TECHNOLOGIES; PERFORMANCE;
D O I
10.1016/j.fuel.2010.12.022
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
080707 [能源环境工程]; 082001 [油气井工程];
摘要
Starting from an equilibrium model for gasification, this research group has devised a new mathematical model, the so called Gibbs Free Energy Gradient Method Model (GMM). This model permits to bypass the semi-qualitative view, typical of equilibrium models, which assume very restrictive hypotheses such as equilibrium state for all the reactions involved in gasification process, complete conversion of carbon matter, gasification products in gas phase only. GMM model overcomes these limitations providing a quantitative point of view, even though the hypothesis of no tar production affects both models. GMM model has been applied to RDF gasification, supplying reliable results in the gasification process analysis. Model computations in terms of gas yield, gas composition, low heating value and H-2 yield, have been compared with literature results, showing that computed data are in good agreement with experimental ones. (C) 2010 Elsevier Ltd. All rights reserved.
引用
收藏
页码:1402 / 1407
页数:6
相关论文
共 21 条
[1]
[Anonymous], 1998, BIOMASS GASIFIER TAR
[2]
Gasification process of wastes containing PVC [J].
Borgianni, C ;
De Filippis, P ;
Pochetti, F ;
Paolucci, M .
FUEL, 2002, 81 (14) :1827-1833
[3]
THE TECHNICAL AND ECONOMIC-FEASIBILITY OF BIOMASS GASIFICATION FOR POWER-GENERATION [J].
BRIDGWATER, AV .
FUEL, 1995, 74 (05) :631-653
[4]
Renewable fuels and chemicals by thermal processing of biomass [J].
Bridgwater, AV .
CHEMICAL ENGINEERING JOURNAL, 2003, 91 (2-3) :87-102
[5]
Economics of biomass energy utilization in combustion and gasification plants: effects of logistic variables [J].
Caputo, AC ;
Palumbo, M ;
Pelagagge, PM ;
Scacchia, F .
BIOMASS & BIOENERGY, 2005, 28 (01) :35-51
[6]
Cioni M., RDF GASIFICATION CIR
[7]
Performance of CaO and MgO for the hot gas clean up in gasification of a chlorine-containing (RDF) feedstock [J].
Corella, Jose ;
Toledo, Jose M. ;
Molina, Gregorio .
BIORESOURCE TECHNOLOGY, 2008, 99 (16) :7539-7544
[8]
A steady state model of gas-char reactions in a downdraft biomass gasifier [J].
Giltrap, DL ;
McKibbin, R ;
Barnes, GRG .
SOLAR ENERGY, 2003, 74 (01) :85-91
[9]
Thermodynamic equilibrium model and second law analysis of a downdraft waste gasifier [J].
Jarungthammachote, S. ;
Dutta, A. .
ENERGY, 2007, 32 (09) :1660-1669
[10]
Principles of a novel multistage circulating fluidized bed reactor for biomass gasification [J].
Kersten, SRA ;
Prins, W ;
van der Drift, B ;
van Swaaij, WPM .
CHEMICAL ENGINEERING SCIENCE, 2003, 58 (3-6) :725-731