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首页> 外文期刊>Water >DESALINATION PLANTS: AN AUSTRALIA SURVEY
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DESALINATION PLANTS: AN AUSTRALIA SURVEY

机译:海水淡化厂:澳大利亚调查

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摘要

A survey of 46 desalination plants in Australia that have capacities greater then 10 kl_/d was carried out during 2008. Operating plants have a total output of 294ML/d, while the outputs for plants under construction amount to 976ML/d, and for proposed plants 925 ML/d. About half of the current plants are located in Western Australia, but by the year 2013 plants will be more evenly distributed across the States.rnThe volumes of feed sources to be utilised are 86% seawater, 1.2% brackish water and 12% industrial effluent. The water recoveries vary from 20-42% for a seawater feed to usually 61-95% for brackish and low salinity feed waters. The total current desalted water usage is dominated by potable supplies (153 ML/d) and 141 ML/d is used for industrial purposes. By the year 2013 the '"desalinated water supply will rise to 1734 ML/d for potable and 461 ML/d for industrial use.rnThe product water cost per kL is mostly in the range of less than $1.25 for potable water and $1.25-$2.00 for industrial water. Of the total water consumption in Australia of 51.5 GL/d in 2004-05, the amount of desalted water in 2008 is 0.294 GL/d, or 0.57% of that total. This will to rise to 4.3% in the year 2013. Waste disposal of the reject salt solution to various environments includes most of it to the sea, although more plants of smaller output use evaporating basins or send the waste to a sewer. Ground infiltration is another option used in some localities.rnIn reverse osmosis process, membrane fouling remains a problem in that it shortens membrane life and increases the cost of the desalination process. Pre-treatment of the feed is required to minimise fouling. Conventional clarification is commonly used, but microfiltration (MF) or ultrafiltration (UF) with membranes is also employed.rnThe average energy consumption is 3-3.7 kWh/kL for sea water RO, 0.7-1 kWh/kL for brackish water and 1.2 kWh/kL for industrial effluent. The total current power used is 30.1 MW, or 722rnMWh/d. By the year 2013 the total power required for the increased desalination capacity in the country will be 277MW.rnThe existing trend towards desalted supplies for municipal and industrial purposes is likely to continue, as climate change effects become more pronounced across the southern part of the Australian continent and the prospect of running out of water becomes more evident. Water reclamation, most notably by industry, will be essential.
机译:在2008年期间,对澳大利亚的46座产能大于10千升/天的海水淡化厂进行了调查。运营工厂的总产量为294毫升/天,而在建工厂的总产量为976毫升/天。植物925毫升/天。目前约有一半的工厂位于西澳大利亚州,但到2013年,这些工厂将在美国各州分布更均匀。饲料来源的使用量为86%的海水,1.2%的微咸水和12%的工业废水。水的回收率从海水饲料的20-42%到咸咸水和低盐度给水的通常61-95%不等。当前淡水的总使用量主要由饮用水(153 ML / d)和141 ML / d用于工业目的。到2013年,饮用水的“淡化水”供应量将增加到1734 ML / d,工业用途的去离子水供应量将上升到461 ML /d。rn每千升的产品水成本大部分在低于1.25美元的饮用水和1.25-2.00美元的范围内工业用水:在2004-05年度澳大利亚的总用水量为51.5 GL / d中,2008年的淡化水量为0.294 GL / d,即占总消耗量的0.57%,在2004年将上升至4.3%。 2013年。废弃物盐溶液在各种环境中的废物处理大部分包括在海中,尽管更多产量较小的工厂使用蒸发池或将废物发送到下水道;在某些地区,地面渗透是另一种选择。渗透过程中,膜结垢仍然是一个问题,因为它会缩短膜的寿命并增加脱盐过程的成本;需要对进料进行预处理以最大程度地减少结垢。通常使用常规澄清方法,但采用微滤(MF)或超滤(UF) )与膜海水RO的平均能耗为3-3.7 kWh / kL,微咸水的平均能耗为0.7-1 kWh / kL,工业废水的平均能耗为1.2 kWh / kL。使用的总当前功率为30.1 MW,即722rnMWh / d。到2013年,该国增加海水淡化能力所需的总电力将达到277MW。rn随着澳大利亚南部地区气候变化的影响变得更加明显,用于市政和工业用途的淡化供应的现有趋势可能会继续。大陆和缺水的前景更加明显。水的再生,尤其是工业再生,将是必不可少的。

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  • 来源
    《Water》 |2009年第2期|67-73|共7页
  • 作者单位

    CSIRO Materials Science and Engineering, Private Bag 33, Clayton South, Vic 3169;

    CSIRO Water for a Healthy Country National Research Flagship, PMB 2, Glen Osmond, SA 5064;

    UNESCO Centre for Membrane Science and Technology, University of NSW, Sydney, NSW 2052;

    Institute of Sustainability and Innovation, Victoria University, PO Box 14428, Melbourne, Vic 8001;

    UNESCO Centre for Membrane Science and Technology, University of NSW, Sydney, NSW 2052;

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