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Economic, energy and carbon footprint assessment of integrated forward osmosis membrane bioreactor (FOMBR) process in urban wastewater treatment
被引:0
|作者:
Ab Hamid, Nur Hafizah
[1
]
Smart, Simon
[1
]
Wang, David K.
[2
]
Koh, Kaniel Wei Jun
[1
,3
]
Ng, Kalvin Jiak Chern
[1
,3
]
Ye, Liu
[1
]
机构:
[1] Univ Queensland, Sch Chem Engn, Brisbane, Qld 1072, Australia
[2] Univ Sydney, Sch Chem & Biomol Engn, Sydney, NSW 2006, Australia
[3] Ngee Ann Polytech, Singapore 599489, Singapore
基金:
澳大利亚研究理事会;
关键词:
NITROGEN REMOVAL;
ANAMMOX;
EMISSIONS;
SEWAGE;
RECOVERY;
HYBRID;
SYSTEM;
MBR;
FO;
D O I:
10.1039/c9ew00608g
中图分类号:
X [环境科学、安全科学];
学科分类号:
08 ;
0830 ;
摘要:
The application of forward osmosis (FO) membrane-based technology in urban wastewater treatment has received increased attention, however, its techno-economic feasibility and sustainability have not been fully demonstrated. In this study, the feasibility of FO application in urban wastewater treatment was assessed in terms of economic performance, energy consumption and greenhouse gas (GHG) emissions benchmarked against microfiltration (MF). Three different scenarios of wastewater treatment and water reclamation were proposed: (A) forward osmosis aerobic membrane bioreactor (FOAeMBR); (B) FOAeMBR integrated with reverse osmosis (RO); (C) forward osmosis anaerobic membrane bioreactor (FOAnMBR) integrated with partial nitrification/anammox (PN/AMOX) process. In this study, the wastewater treatment and reclamation costs by using FO in scenarios A and B were more expensive than MF by $0.16 per m(3) and $0.75 per m(3) respectively due to the larger surface area of FO membrane required. In scenario C, the wastewater treatment cost of using FO ($1.11 per m(3)) was equivalent to MF. This was due to the good rejection performance of FO and its ability to concentrate wastewater, hence, resulting in a higher efficiency of (PN/AMOX) in comparison to MF. In addition, the application of FO in scenario C generated total GHG emissions to be as low as 0.93 kg CO2 equivalent m(-3), which was 1.5 and 4.1 times lower than scenarios A and B respectively. The minimal net energy consumption and low carbon footprint of FO application in scenario C suggests this integration will likely be a feasible membrane-based technology for the next generation of wastewater treatment.
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页码:153 / 165
页数:13
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