首页> 外文期刊>Desalination and water treatment >Recent development in thermally activated desalination methods: achieving an energy efficiency less than 2.5 kWh(elec)/m(3)
【24h】

Recent development in thermally activated desalination methods: achieving an energy efficiency less than 2.5 kWh(elec)/m(3)

机译:热活化淡化方法的最新进展:能源效率低于2.5 kWh(elec)/ m(3)

获取原文
获取原文并翻译 | 示例
       

摘要

Water-Energy-Environment nexus is a crucial consideration when designing seawater desalination processes, particularly for the water-stressed countries where the annual water availability is less than 250 m(3) per capita. Despite the thermodynamics limit for seawater desalination at normal conditions is about 0.78 to 1.09 kWh(elec)/m(3), the specific energy consumption of desalination of real plants is found to operate at several folds higher. Today's technological advancement in membranes, namely the reverse osmosis processes, has set an energy consumption of around 3.5-5 kWh(elec)/m(3), while the conventional perception of thermally activated processes such as MSF and MED tends to be higher. Although the higher energetic specific consumption of MED or MSF processes appeared to be higher at 60-100 kWh(thermal)/m(3), their true electricity equivalent has been converted, hitherto, using the energetic analyses where the work potential of working steam of the processes cannot be captured adequately. Thermally activated processes, such as MED and MSF, form the bottoming cycle of a cogeneration plant where both electricity and desalination processes operate in tandem in a cascaded manner. Only the bled-steam at lower exergy is extracted for the desalination processes. In this presentation, we demonstrate that in a cogen plant with 30% bled-steam for MED processes, the exergy destruction ratio is found to be less than 7% of the total available exergy that emanated from the boilers. By the exergetic approach, the equivalent electricity consumption of an average 75 kWh(thermal)/m(3) would result in an electrical equivalent of less than 2.5 kWh(elec)/m(3). Also in this presentation, the authors will elaborate the latest developments in the use of hybridization concept where the MED and the AD cycles are thermodynamically integrated and enhancing the overall efficiency of desalination.
机译:在设计海水淡化工艺时,水-能源-环境之间的联系是至关重要的考虑因素,特别是对于人均年用水量少于250 m(3)的缺水国家而言。尽管在正常条件下海水淡化的热力学极限约为0.78至1.09 kWh(elec)/ m(3),但发现实际植物的海水淡化的单位能耗要高出几倍。当今膜技术的进步,即反渗透工艺,已将能量消耗定为约3.5-5 kWh(elec)/ m(3),而热活化工艺(如MSF和MED)的传统认识往往更高。尽管MED或MSF过程的高能比消耗似乎更高,为60-100 kWh(热)/ m(3),但迄今为止,已使用能量分析将其真实电当量进行了换算,其中工作蒸汽的工作潜力的过程不能被充分捕获。诸如MED和MSF之类的热活化过程形成了热电联产工厂的底部循环,在此期间,电力和脱盐过程均以级联的方式串联运行。仅将较低火用的放气蒸汽用于脱盐过程。在本演示中,我们证明了在有30%放气蒸汽用于MED工艺的热电联产工厂中,火用破坏率小于锅炉产生的全部可用火用的7%。通过积极的方法,平均75 kWh(热)/ m(3)的等效电力消耗将导致小于2.5 kWh(elec)/ m(3)的等效电力。同样在本演示文稿中,作者将阐述杂交概念的最新发展,在杂交概念中,MED和AD循环进行了热力学整合,并提高了脱盐的整体效率。

著录项

相似文献

  • 外文文献
  • 中文文献
  • 专利
获取原文

客服邮箱:kefu@zhangqiaokeyan.com

京公网安备:11010802029741号 ICP备案号:京ICP备15016152号-6 六维联合信息科技 (北京) 有限公司©版权所有
  • 客服微信

  • 服务号