Recovery of Freshwater from Wastewater: Upgrading Process Configurations To Maximize Energy Recovery and Minimize Residuals

被引:77
作者
Scherson, Yaniv D. [1 ,2 ]
Criddle, Craig S. [1 ,2 ]
机构
[1] Stanford Univ, Dept Civil & Environm Engn, Stanford, CA 94305 USA
[2] Stanford Univ, Woods Inst Environm, NSF Engn Res Ctr ReNUWIt, Dept Civil & Environm Engn, Stanford, CA 94305 USA
基金
美国国家科学基金会;
关键词
AUTOTROPHIC NITROGEN-REMOVAL; FULL-SCALE APPLICATION; MICROBIAL FUEL-CELLS; DRIED SEWAGE-SLUDGE; MEMBRANE BIOREACTORS; ANAEROBIC-DIGESTION; SUPERCRITICAL WATER; BIOSOLIDS DIGESTION; INNOVATIVE METHOD; SHARON PROCESS;
D O I
10.1021/es501701s
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
Analysis of conventional and novel wastewater treatment configurations reveals large differences in energy consumed or produced and solids generated per cubic meter of domestic wastewater treated. Complete aerobic BOD removal consumes 0.45 kWh and produces 153 g of solids, whereas complete anaerobic treatment produces 0.25 kWh and 80 g of solids. Emerging technologies, that include short-circuit nitrogen removal (SHARON, CANON with Anammox, CANDO) and mainstream anaerobic digestion, can potentially remove both BOD and nitrogen with an energy surplus of 0.17 kWh and production of 95 g of solids. Heat from biogas combustion can completely dry the solids, and these solids can be converted to syngas without imported energy. Syngas combustion can produce similar to 0.1 kWh with an inorganic residue of just 10 g. If salt is removed, freshwater can be recovered with net production of electrical energy from methane (0.03-0.13 kWh) and syngas (similar to 0.1 kWh) and an inorganic residue of similar to 0.1-0.3 kg as brine. Current seawater desalination requires 3-4 kWh (thermodynamic limit of 1 kWh) and results in an inorganic residue of similar to 35 kg as brine.
引用
收藏
页码:8420 / 8432
页数:13
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