Assessing the bioenergy potential of high-ash anaerobic sewage sludge using pyrolysis kinetics and thermodynamics to design a sustainable integrated biorefinery

被引:25
作者
Alves, Jose Luiz Francisco [1 ]
da Silva, Jean Constantino Gomes [1 ]
Languer, Mariana Pires [1 ]
Batistella, Luciane [2 ]
Di Domenico, Michele [3 ]
da Silva Filho, Valdemar Francisco [1 ]
Moreira, Regina de Fatima Peralta Muniz [1 ]
Jose, Humberto Jorge [1 ]
机构
[1] Univ Fed Santa Catarina, Dept Chem Engn & Food Engn, Grad Program Chem Engn, BR-88040900 Florianopolis, SC, Brazil
[2] Fed Univ Southern & Southeastern Para, Inst Geosci & Engn, BR-68507590 Maraba, Para, Brazil
[3] Fed Univ Technol Parana UTFPR Francisco Beltrao, Dept Engn, BR-85601970 Francisco Beltrao, Parana, Brazil
关键词
Sewage sludge; Bioenergy potential; Pyrolysis kinetics; Thermodynamic evaluation; Sustainable biorefinery; TG-FTIR-MS; GASEOUS EMISSIONS; DOMESTIC SEWAGE; ENERGY; GASIFICATION; COMBUSTION; CHALLENGES; PARAMETERS; DIGESTION; WASTE;
D O I
10.1007/s13399-020-01023-2
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
A new opportunity for producing valuable biorefinery products can be found by integrating biochemical and thermochemical processing with municipal wastewater treatment. This study is the first to evaluate the kinetic triplet and thermodynamic parameters from the pyrolysis of typical Brazilian anaerobic sewage sludge performed in the framework of a multi-step solid-state process. The physicochemical characteristics of the anaerobic sewage sludge are comparable to those obtained from low-rank coals. The pyrolysis characteristics were analyzed by non-isothermal thermogravimetry under different heating rates (10, 25, 50, and 90 K min(-1)) in an inert atmosphere. Two devolatilization stages were distinguished from the active pyrolysis zone, with an average mass loss of 47.56 wt% (sum) in the range of 398-953 K. For each devolatilization stage, three isoconversional methods (Flynn-Wall-Ozawa, Kissinger-Akahira-Sunose, and Starink) were utilized to calculate the activation energy, and then the compensation effect method was applied to find the pre-exponential factor. The average activation energies calculated ranged from 113.7 to 117.3 kJ mol(-1) for the first stage and from 115.7 to 121.9 kJ mol(-1) for the second stage, with respective pre-exponential factors of 7.39 x 10(9) min(-1)and 8.80 x 10(7)min(-1). According to the master-plots method, it was found that the first stage followed the fourth-order (F4) model, while the second stage was described by the second-order (F2) model. Based on the statistical evaluation, the devolatilization behaviors reconstructed from overall kinetic expression agree reasonably well with the experimental data, proving its practical importance for designing a pyrolytic processing system using anaerobic sewage sludge as raw material. This study contributes by providing useful insights that can be applied to a large-scale biorefinery as a critical step towards producing biofuels coupled to municipal wastewater treatment in an environmentally sustainable manner.
引用
收藏
页码:693 / 704
页数:12
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