Pilot demonstration of concentrated solar-powered desalination of subsurface agricultural drainage water and other brackish groundwater sources

被引:35
|
作者
Stuber, Matthew D. [1 ]
Sullivan, Christopher [2 ]
Kirk, Spencer A. [2 ]
Farrand, Jennifer A. [2 ]
Schillaci, Philip V. [2 ]
Fojtasek, Brian D. [2 ]
Mandell, Aaron H. [1 ]
机构
[1] WaterFX Inc, Healdsburg, CA 95448 USA
[2] ATSI Inc, Amherst, NY 14228 USA
关键词
Solar desalination; MED; Energy efficiency; Absorption heat pump; Renewable energy; ABSORPTION HEAT-PUMP; ADSORPTION DESALINATION; EFFECT EVAPORATION; VAPOR COMPRESSION; STRUCTURAL OPTIMIZATION; WASTE HEAT; SEAWATER; SYSTEMS; MSF; CONFIGURATIONS;
D O I
10.1016/j.desal.2014.10.037
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
The energy-water nexus is addressed with the experimental demonstration of a solar-powered desalination process system. This system was designed for high-recovery treatment of subsurface agricultural drainage water as a reuse strategy as well as other brackish groundwater sources. These water sources may exhibit wide fluctuations in salinity and makeup and pose a high risk for operational troubles due to high scaling potential. A first-of-itskind open-cycle vapor-absorption heat pump is coupled with a multiple-effect distillation train and a large parabolic trough solar thermal concentrator. Without the heat pump, the distillation operation showed a minimum thermal energy consumption of 261.87 kWh(th)/m(3). With the heat pump, the thermal energy consumption was reduced by more than 49% to 133.2 kWh(th)/m(3). This reduction in thermal energy requirement directly translates into a 49% reduction in solar array area required to power a process with the same freshwater production rate as a system without an integrated heat pump. An optimized design was modeled and the thermal energy performance of a commercial system is projected at 34.9 kVVh(th)/m(3) using a 10-effect MED operating at 85% recovery. (C) 2014 Elsevier B.V. All rights reserved.
引用
收藏
页码:186 / 196
页数:11
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