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A novel conceptual design of hydrate based desalination (HyDesal) process by utilizing LNG cold energy

机译:利用LNG冷能的水合物脱盐(HyDesal)工艺的新颖概念设计

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Liquefied Natural Gas (LNG) is the best mode to transport natural gas from producing locations to importing countries when pipeline transport is not feasible. LNG industry has seen a phenomenal growth due to the widespread adoption of natural gas as a clean fuel. There is an ongoing effort to develop new technologies that can utilize LNG cold energy which is mostly being wasted at the LNG regasification terminals around the world. This work presents a novel conceptual design for a clathrate hydrate based desalination (HyDesal) process by utilizing LNG cold energy (ColdEn-HyDesal). This ColdEn-HyDesal process overcomes the high energy consumption of the traditional HyDesal process by using the cold energy of LNG to replace the external refrigeration cycle. An optimal heat exchanger network for the ColdEn-HyDesal process is obtained by employing mathematical programming based heat integration methodology for the LNG flow rate of 1000 kg/h in an LNG regasification terminal. The results indicate that the specific energy consumption (SEC) of the HyDesal process is 65.29 kWh/m(3) of potable water, while that of the ColdEn-HyDesal process is only 0.60 kWh/m(3) when the hydrate former is not recycled. When the hydrate former is recycled, then the specific energy consumption of the HyDesal process is 65.13 kWh/m(3), while that of the ColdEn-HyDesal process is only 0.84 kWh/m(3). In addition, the effects of recovery pressure, water recovery rate, and NaCl concentration in seawater on SEC and the volumetric rate of potable water are also analyzed and discussed. The results show that the SEC decreases substantially (27.42%) with the increase of water recovery from 40% to 70% in one hour. Further, the NaCl concentration in the feed has a small impact on the SEC, which only increases by 2.81% when the NaCl concentration increases from 3.5 wt% to 7.0 wt%. Thus, the ColdEn-HyDesal process is an energy efficient desalination process and can be a potential technology to desalinate seawater, and high concentration brines in an LNG regasification terminal.
机译:当管道运输不可行时,液化天然气(LNG)是将天然气从生产地运输到进口国的最佳方式。由于天然气被广泛用作清洁燃料,液化天然气行业出现了惊人的增长。正在进行开发可利用LNG冷能的新技术的努力,该技术主要在世界各地的LNG再气化站被浪费。这项工作为利用LNG冷能(ColdEn-HyDesal)的基于笼形水合物的脱盐(HyDesal)工艺提出了一种新颖的概念设计。通过使用液化天然气的冷能代替外部制冷循环,该ColdEn-HyDesal工艺克服了传统HyDesal工艺的高能耗。通过对LNG再气化终端中1000 kg / h的LNG流量采用基于数学程序的热集成方法,可获得用于ColdEn-HyDesal工艺的最佳热交换器网络。结果表明,HyDesal工艺的单位能耗(SEC)为65.29 kWh / m(3)饮用水,而ColdEn-HyDesal工艺的单位能耗仅为0.60 kWh / m(3)。回收的。当水合物前体被循环利用时,HyDesal工艺的单位能耗为65.13 kWh / m(3),而ColdEn-HyDesal工艺的单位能耗仅为0.84 kWh / m(3)。此外,还分析和讨论了回收压力,回收率和海水中NaCl浓度对SEC和饮用水体积率的影响。结果表明,在一小时内,随着水的回收率从40%增加到70%,SEC显着降低(27.42%)。此外,进料中的NaCl浓度对SEC的影响很小,当NaCl浓度从3.5 wt%增加到7.0 wt%时,SEC仅增加2.81%。因此,ColdEn-HyDesal工艺是一种节能的海水淡化工艺,可以成为在LNG再气化终端中使海水和高浓度盐水脱盐的潜在技术。

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