TGA pyrolysis and gasification of combustible municipal solid waste

Abstract It brings modeling, design and operation of thermochemical treatment systems a huge challenge for a large variety in municipal solid waste (MSW) composition and differences in thermal behavior of MSW components. The pyrolysis and gasification characteristics of 8 different combustible solid wastes, representing the most common components of MSW, were investigated using a thermogravimetric analyzer (TGA). Their decomposed characteristics in different atmospheres (N 2 and CO 2 ) was analyzed and compared, which identified as pyrolysis and gasification, respectively. The results showed that pyrolysis characteristics of 8 materials were similar to their gasification with the temperature less than 600 °C. The pyrolysis degradation of eight materials was slight above 600 °C, while the gasification degradation in the range of 700–900 °C was obvious because of the reaction between CO 2 and char. The discrete distributed activation energy method (DAEM) was applied to analyze kinetics of pyrolysis and gasification. When pre-exponential factor was given as 2.2 × 10 13 (s −1 ), the activation energy of cellulose decomposed reaction was approximately 176 kJ/mol, while the activation energy of the reaction between CO 2 and char was 327 kJ/mol.

[1]  Yirong Liu,et al.  Pyrolysis of polystyrene waste in a fluidized-bed reactor to obtain styrene monomer and gasoline fraction , 2000 .

[2]  An Dawei,et al.  Low-temperature pyrolysis of municipal solid waste: influence of pyrolysis temperature on the characteristics of solid fuel , 2006 .

[3]  C. Blasi,et al.  Critical evaluation of global mechanisms of wood devolatilization , 2005 .

[4]  M. Ni,et al.  Pyrolysis characteristics of organic components of municipal solid waste at high heating rates. , 2009, Waste management.

[5]  J. Gore,et al.  Experimental and modeling study of pinewood char gasification with CO2 , 2014 .

[6]  J. Balmaseda,et al.  Pyrolysis of orange waste: A thermo-kinetic study , 2013 .

[7]  H. Spliethoff,et al.  TG-FTIR pyrolysis of coal and secondary biomass fuels: Determination of pyrolysis kinetic parameters for main species and NOx precursors , 2007 .

[8]  J. Hustad,et al.  Pyrolysis characteristics and kinetics of municipal solid wastes , 2001 .

[9]  K. Miura A New and Simple Method to Estimate f(E) and k0(E) in the Distributed Activation Energy Model from Three Sets of Experimental Data , 1995 .

[10]  Alan K. Burnham,et al.  Analysis of chemical reaction kinetics using a distribution of activation energies and simpler models , 1987 .

[11]  E. Kwon,et al.  Urban energy mining from municipal solid waste (MSW) via the enhanced thermo-chemical process by carbon dioxide (CO2) as a reaction medium. , 2012, Bioresource technology.

[12]  Cen Ke-fa,et al.  Pyrolysis behavior of cellulose,xylan and lignin , 2006 .

[13]  J. A. Conesa,et al.  Comments on the validity and utility of the different methods for kinetic analysis of thermogravimetric data , 2001 .

[14]  Jacopo Giuntoli,et al.  Quantitative and kinetic TG-FTIR study of biomass residue pyrolysis: Dry distiller's grains with solubles (DDGS) and chicken manure , 2009 .

[15]  K. Miura,et al.  A Simple Method for Estimating f(E) and k0(E) in the Distributed Activation Energy Model , 1998 .

[16]  Panagiotis Grammelis,et al.  Kinetic Modeling of Coal/Agricultural By-Product Blends , 2003 .

[17]  Zhiquan Hu,et al.  Effect of particle size on pyrolysis of single-component municipal solid waste in fixed bed reactor , 2010 .

[18]  Paul T. Williams,et al.  Pyrolysis of waste materials using TGA-MS and TGA-FTIR as complementary characterisation techniques , 2012 .

[19]  Michael Jerry Antal,et al.  Thermal Lag, Fusion, and the Compensation Effect during Biomass Pyrolysis† , 1996 .

[20]  Weihong Yang,et al.  Gasification of municipal solid waste in the Plasma Gasification Melting process , 2012 .

[21]  Qinghai Li,et al.  An overview of characteristics of municipal solid waste fuel in China: Physical, chemical composition and heating value , 2014 .

[22]  Qinghai Li,et al.  The pyrolysis simulation of five biomass species by hemi-cellulose, cellulose and lignin based on thermogravimetric curves , 2013 .

[23]  Peter McKendry,et al.  Energy production from biomass (Part 1): Overview of biomass. , 2002, Bioresource technology.

[24]  R. Pelet,et al.  Extrapolation of the kinetics of oil and gas formation from laboratory experiments to sedimentary basins , 1987, Nature.

[25]  Colomba Di Blasi,et al.  Combustion and gasification rates of lignocellulosic chars , 2009 .