Supercritical water gasification of wastewater sludge for hydrogen production

被引:113
作者
Ibrahim, A. B. A. [1 ]
Akilli, H. [2 ]
机构
[1] Univ Blue Nile, Dept Mech Engn, Fac Engn, Al Dmazin, Sudan
[2] Cukurova Univ, Fac Arch & Engn, Dept Mech Engn, Adana, Turkey
关键词
Supercritical water gasification; Biomass; Wastewater sludge; Syngas; Hydrogen; Operation parameters; CATALYTIC HYDROTHERMAL GASIFICATION; DEWATERED SEWAGE-SLUDGE; PARTIAL OXIDATIVE GASIFICATION; PRESSURE AQUEOUS ENVIRONMENTS; FLUIDIZED-BED REACTOR; HOT COMPRESSED WATER; BIOMASS GASIFICATION; SUBCRITICAL WATER; CONTINUOUS-FLOW; HIGH-TEMPERATURE;
D O I
10.1016/j.ijhydene.2019.02.184
中图分类号
O64 [物理化学(理论化学)、化学物理学];
学科分类号
070304 ; 081704 ;
摘要
The use of hydrogen as clean fuel gas in the power generation sector becomes essential to reduce the environmental issues related to conventional fuel usage. By avoiding biomass drying process, supercritical water gasification is considered the most efficient technology in hydrogen production from wastewater sludge. Wastewater sludge is difficult to disposal in its received form since it is often produced with high moisture content, contribute to numerous environmental issues and direct contact with this waste can result in health concerns. The assessment of the treatment and conversion of this material into fuel gas at condition beyond supercritical state (374 degrees C and 22.1 MPa) is required. This paper is discussed the degradation routes of wastewater sludge in supercritical water. Furthermore, it is reviewed the influence of the main operation parameters role in the hydrogen production, which includes reaction temperature, pressure, residence time, feed concentration and catalysts. The development in reactor design and setup for maximum hydrogen production is highlighted. The technical challenges encountered during the conversion process and its solutions are also discussed. In addition, future prospective to optimal and standardization of the supercritical water gasification process is reviewed. (C) 2019 Hydrogen Energy Publications LLC. Published by Elsevier Ltd. All rights reserved.
引用
收藏
页码:10328 / 10349
页数:22
相关论文
共 251 条
[91]   Products evolution during hydrothermal conversion of dewatered sewage sludge in sub- and near-critical water: Effects of reaction conditions and calcium oxide additive [J].
He, Chao ;
Wang, Ke ;
Giannis, Apostolos ;
Yang, Yanhui ;
Wang, Jing-Yuan .
INTERNATIONAL JOURNAL OF HYDROGEN ENERGY, 2015, 40 (17) :5776-5787
[92]   Hydrothermal gasification of sewage sludge and model compounds for renewable hydrogen production: A review [J].
He, Chao ;
Chen, Chia-Lung ;
Giannis, Apostolos ;
Yang, Yanhui ;
Wang, Jing-Yuan .
RENEWABLE & SUSTAINABLE ENERGY REVIEWS, 2014, 39 :1127-1142
[93]   Exploration of the effect of process variables on the production of high-value fuel gas from glucose via supercritical water gasification [J].
Hendry, Doug ;
Venkitasamy, Chandrasekar ;
Wilkinson, Nikolas ;
Jacoby, William .
BIORESOURCE TECHNOLOGY, 2011, 102 (03) :3480-3487
[94]  
Herzog A.V., 2001, RENEWABLE ENERGY SOU
[95]  
HEUKELEKIAN H, 1959, SEWAGE IND WASTES, V31, P413
[96]   GLUCOSE HYDROLYSIS AND OXIDATION IN SUPERCRITICAL WATER [J].
HOLGATE, HR ;
MEYER, JC ;
TESTER, JW .
AICHE JOURNAL, 1995, 41 (03) :637-648
[97]   Production of H2 from microalgae biomass in supercritical water using a Ni/La-γAl2O3 catalyst [J].
Hossain, Mohammad M. .
1ST INTERNATIONAL CONFERENCE ON ENERGY AND POWER, ICEP2016, 2017, 110 :384-389
[98]   A review on biomass-based hydrogen production for renewable energy supply [J].
Hosseini, Seyed Ehsan ;
Wahid, Mazlan Abdul ;
Jamil, M. M. ;
Azli, Anis A. M. ;
Misbah, Mohamad F. .
INTERNATIONAL JOURNAL OF ENERGY RESEARCH, 2015, 39 (12) :1597-1615
[99]   Raney Ni-Sn catalyst for H2 production from biomass-derived hydrocarbons [J].
Huber, GW ;
Shabaker, JW ;
Dumesic, JA .
SCIENCE, 2003, 300 (5628) :2075-2077
[100]   Intermediates and kinetics for phenol gasification in supercritical water [J].
Huelsman, Chad M. ;
Savage, Phillip E. .
PHYSICAL CHEMISTRY CHEMICAL PHYSICS, 2012, 14 (08) :2900-2910