Pyrolytic characteristics of sewage sludge

被引:118
作者
Thipkhunthod, Puchong
Meeyoo, Vissanu
Rangsunvigit, Pramoch
Kitiyanan, Boonyarach
Siemanond, Kitipat
Rirksomboon, Thirasak
机构
[1] Mahanakorn Univ Technol, Ctr Adv Mat & Environm Res, Bangkok 10530, Thailand
[2] Chulalongkorn Univ, Petr & Petrochem Coll, Bangkok 10330, Thailand
关键词
sewage sludge; pyrolysis; kinetics;
D O I
10.1016/j.chemosphere.2006.01.002
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
In this study, a number of different sewage sludge including sludge samples from industrial and hospital wastewater treatment plants were characterized for pyrolysis behavior by means of thermogravimetric analysis up to 800 degrees C. According to the thermogravimetric results, five different types of mass loss behaviors were observed depending on the nature of the sludge used. Typical main decomposition steps occurred between 250 and 550 degrees C although some still decomposed at higher temperatures. The first group (Types I, II and III) was identified by main decomposition at approximately 300 degrees C and possible second reaction at higher temperature. Differences in the behavior may be due to different components in the sludge both quantitatively and qualitatively. The second group (Types IV and V), which rarely found, has unusual properties. DTG peaks were found at 293, 388 and 481 degrees C for Type IV and 255 and 397 degrees C for Type V. Kinetics of sludge decomposition can be described by either pseudo single or multicomporient overall models (PSOM or PMOM). The activation energy of the first reaction, corresponding to the main pyrolysis typically at 300 degrees C, was rather constant (between 68 and 77 kJ mol(-1)) while those of second and third reactions were varied in the range of 85-185 kJ mol(-1). The typical order of pyrolysis reaction was in the range of 1.1-2.1. The pyrolysis gases were composed of both saturated and unsaturated light hydrocarbons, carbon dioxide, ethanol and chloromethane. Most products, however, evolve at a quite similar temperature regardless of the sludge type. (c) 2006 Elsevier Ltd. All rights reserved.
引用
收藏
页码:955 / 962
页数:8
相关论文
共 30 条
[21]   Analysis of the co-combustion of sewage sludge and coal by TG-MS [J].
Otero, M ;
Díez, C ;
Calvo, LF ;
García, AI ;
Morán, A .
BIOMASS & BIOENERGY, 2002, 22 (04) :319-329
[22]   Pyrolytic characteristics of microalgae as renewable energy source determined by thermogravimetric analysis [J].
Peng, WM ;
Wu, QY ;
Tu, PG ;
Zhao, NM .
BIORESOURCE TECHNOLOGY, 2001, 80 (01) :1-7
[23]   Thermal analysis for the evaluation of the organic matter evolution during municipal solid waste aerobic composting process [J].
Pietro, M ;
Paola, C .
THERMOCHIMICA ACTA, 2004, 413 (1-2) :209-214
[24]   Pyrolysis of API separator sludge [J].
Punnaruttanakun, P ;
Meeyoo, V ;
Kalambaheti, C ;
Rangsunvigit, P ;
Rirksomboon, T ;
Kitiyanan, B .
JOURNAL OF ANALYTICAL AND APPLIED PYROLYSIS, 2003, 68-9 :547-560
[25]  
SHEN L, 2001, P 6 WORLD C CHEM ENG
[26]   Pyrolysis characteristics and kinetics of municipal solid wastes [J].
Sorum, L ;
Gronli, MG ;
Hustad, JE .
FUEL, 2001, 80 (09) :1217-1227
[27]  
SPEICHT JG, 1994, COAL TECHNOLOGY THEO
[28]   Predicting the heating value of sewage sludges in Thailand from proximate and ultimate analyses [J].
Thipkhunthod, P ;
Meeyoo, V ;
Rangsunvigit, P ;
Kitiyanan, B ;
Siemanond, K ;
Rirksomboon, T .
FUEL, 2005, 84 (7-8) :849-857
[29]   Formation of NOx precursors during the pyrolysis of coal and biomass.: Part V.: Pyrolysis of a sewage sludge [J].
Tian, FJ ;
Li, BQ ;
Chen, Y ;
Li, CZ .
FUEL, 2002, 81 (17) :2203-2208
[30]   Sewage sludge combustion [J].
Werther, J ;
Ogada, T .
PROGRESS IN ENERGY AND COMBUSTION SCIENCE, 1999, 25 (01) :55-116