Energy recovery from secondary pulp/paper-mill sludge and sewage sludge with supercritical water treatment

被引:133
作者
Zhang, Linghong [2 ]
Xu, Chunbao [1 ]
Champagne, Pascale [2 ,3 ]
机构
[1] Lakehead Univ, Dept Chem Engn, Thunder Bay, ON P7B 5E1, Canada
[2] Queens Univ, Dept Civil Engn, Kingston, ON K7L 3N6, Canada
[3] Queens Univ, Dept Chem Engn, Kingston, ON K7L 3N6, Canada
基金
加拿大自然科学与工程研究理事会;
关键词
Secondary pulp/paper-mill sludge; Sewage sludge; Supercritical water; Synthetic gas; Heavy oil; BIOMASS GASIFICATION; HYDROTHERMAL GASIFICATION; CATALYTIC GASIFICATION; HYDROGEN-PRODUCTION; LIQUEFACTION; CONVERSION; HYDROXIDE; PRODUCTS; GAS;
D O I
10.1016/j.biortech.2009.11.106
中图分类号
S2 [农业工程];
学科分类号
0828 ;
摘要
Secondary pulp/paper-mill sludge (SPP) and sewage sludges (primary, secondary, and digested sewage sludges) were treated in supercritical water at temperatures ranging between 400 degrees C and 550 degrees C over 20-120 min for energy recovery. Low temperature and short reaction time favored the formation of heavy oil (HO) products, which were mainly composed of a variety of phenol and phenolic compounds, as well as some nitrogen-containing compounds, long-chain alkenes and alcohols, etc., with high gross calorific values (> 36 MJ/kg). By contrast, the formation of synthetic gases, a mixture of hydrogen, carbon monoxide, carbon dioxide, methane, and other light hydrocarbons, were not significantly affected by reaction time but greatly enhanced with increasing temperature. The highest gas yield was obtained at 550 C, where 37.7 wt.% of the SPP (on dry basis) was converted into gases, with hydrogen yields as high as 14.5 mol H-2/kg SPP (on a dry basis). In comparison to sewage sludges, SPP exhibited a greater capability for the production of HO and gases owing to its higher contents of volatiles and alkali metals, indicating a prospective utilization potential for SPP as a source of bio-energy. (C) 2009 Elsevier Ltd. All rights reserved.
引用
收藏
页码:2713 / 2721
页数:9
相关论文
共 25 条
[1]  
Bridgewater AV., 2001, Thermal conversion of biomass and waste: the status
[2]  
Demirbas A, 2004, INT J HYDROGEN ENERG, V29, P1237, DOI [10.1016/j.ijhydene.2003.11.012, 10.1016/j.ijydene.2003.11.012]
[3]  
Furness DT, 2000, J CHART INST WATER E, V14, P57
[4]   Utilization of sewage sludge in EU application of old and new methods - A review [J].
Fytili, D. ;
Zabaniotou, A. .
RENEWABLE & SUSTAINABLE ENERGY REVIEWS, 2008, 12 (01) :116-140
[5]  
GLOYNA EF, 1994, WATER SCI TECHNOL, V30, P1
[6]   Hydrogen production by biomass gasification in supercritical water: A systematic experimental and analytical study [J].
Guo, L. J. ;
Lu, Y. J. ;
Zhang, X. M. ;
Ji, C. M. ;
Guan, Y. ;
Pei, A. X. .
CATALYSIS TODAY, 2007, 129 (3-4) :275-286
[7]   Biomass conversion in water at 330-410°C and 30-50 MPa.: Identification of key compounds for indicating different chemical reaction pathways [J].
Kruse, A ;
Gawlik, A .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2003, 42 (02) :267-279
[8]   Biomass gasification in supercritical water: Influence of the dry matter content and the formation of phenols [J].
Kruse, A ;
Henningsen, T ;
Sinag, A ;
Pfeiffer, J .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2003, 42 (16) :3711-3717
[9]   Supercritical water gasification [J].
Kruse, Andrea .
BIOFUELS BIOPRODUCTS & BIOREFINING-BIOFPR, 2008, 2 (05) :415-437
[10]   Influence of proteins on the hydrothermal gasification and liquefaction of biomass. 2. Model compounds [J].
Kruse, Andrea ;
Maniam, Palanikumar ;
Spieler, Franziska .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2007, 46 (01) :87-96