Energy Efficient Waste Heat Coupled Forward Osmosis for Effluent Water Management at Coal-Fired Power Plants [electronic resource]

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Tác giả:

Ngôn ngữ: eng

Ký hiệu phân loại: 378.1 Organization and activities in higher education

Thông tin xuất bản: Washington, D.C. : Oak Ridge, Tenn. : United States. Office of the Assistant Secretary of Energy for Fossil Energy ; Distributed by the Office of Scientific and Technical Information, U.S. Dept. of Energy, 2021

Mô tả vật lý: Size: 166 p. : , digital, PDF file.

Bộ sưu tập: Metadata

ID: 267841

 This project sought to evaluate the technical and economic viability of the Aquapod�, a transformational low energy (<
 200 kJ/kg water) waste heat coupled forward osmosis (FO) technology, to manage effluents, meet cooling water demands, and achieve water conservation in a coal-fired power plant environment. The Aquapod� process is innovative because it is heat-driven, avoids the evaporation of water, and uses no toxic chemicals such as ammonia or amines. The Aquapod� process accomplishes this using an aqueous two-phase system (ATPS) coupled FO process. The evaluation revealed that the Aquapod� process offers a pathway to exploit waste heat resources within a power plant to achieve flue-gas desulfurization (FGD) wastewater volume reduction and water recovery with minimal pretreatment. Water recovery of 80% from FGD wastewater was achieved with minimal pretreatment, exceeding the project target of 50%. The estimated electrical energy of 2.16 kWh/m<
 sup>
 3<
 /sup>
  of water produced for the Aquapod� process met the project target of <
  3.6 kWh/m<
 sup>
 3<
 /sup>
 . The heat required for the process operation was approximately 186 kJ/kg of produced water, which was slightly lower than the project target of 200 kJ/kg. The estimated treatment cost for installing and operating the Aquapod� process in conjunction with a spray dryer evaporator to achieve zero-liquid discharge (ZLD) of the 100 gpm FGD wastewater was $13.24/m<
 sup>
 3<
 /sup>
  over a 30-year lifetime. As a point of reference, this study?s host power plant currently incurs a cost of $3.70/m<
 sup>
 3<
 /sup>
  ? $8.87/m3 on a discharged volume basis to discharge its wastewater into the publicly owned treatment works (POTW) after physical-chemical treatment. Therefore, the Illinois power plant would incur an incremental cost increase of $4.37/m<
 sup>
 3<
 /sup>
  ? 9.54/m<
 sup>
 3<
 /sup>
  to achieve ZLD using the Aquapod� and spray dryer combination. Ample opportunities exist to further lower the ZLD capital and operating costs in the next design iteration to attain pipe parity at the higher end of the site treatment costs.
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