INDUSTRIAL RECYCLE TOWARDS ZERO DISCHARGE - Alumina Refinery Case Study

Q. Mortley, W. Mellowes
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Abstract

: Water management at alumina refineries and associated power plants is a major concern, especially if water resources are scarce and liquid discharges are not permitted. This paper describes the case of one such plant in Jamaica recovering 350 m 3 /h of digester regenerative condensate. The steam and power for the alumina refinery is supplied by a cogeneration facility, which has to use a mix of well water and return condensate from the steam users in the alumina production process. The refinery produces alumina from Jamaican bauxite ore, using the Bayer process. This process includes the digestion of bauxite with sodium hydroxide at 135 deg.C, hence the requirement for both steam and power. In the course of this extraction, large quantities (350 m 3 /h) of digester and evaporator condensate are produced. In view of the limited liquid discharges permitted from the site, this condensate was stored on site in large ponds, and reused in the process. Pressured from three sides, with a limitation on raw water abstraction from the wells by the Water Resource Authority, a requirement for minimized liquid discharge of wastewater, and high cost of energy there was a need to utilize the regenerative condensate from the digesters and the evaporators as boiler feedwater. Studies carried out by international water treatment companies had concluded that Total Organic Carbon (TOC) would not allow condensate re-use as boiler feedwater, with an attached US$10 million cost for the removal of TOC. Extensive laboratory work and thermodynamic analysis were carried out and the condensate are used as boiler feedwater, without treatment. The avoided cost was US$10 million and energy savings of US$3 million realized.
工业回收迈向零排放-氧化铝精炼厂案例研究
:氧化铝精炼厂和相关发电厂的水管理是一个主要问题,特别是在水资源稀缺和不允许排放液体的情况下。本文介绍了在牙买加的一个这样的工厂回收350立方米/小时的消化池再生冷凝水的情况。氧化铝精炼厂的蒸汽和动力由热电联产设施提供,该设施在氧化铝生产过程中必须使用井水和蒸汽用户返回的冷凝水的混合物。这家精炼厂采用拜耳工艺,从牙买加铝土矿矿石中生产氧化铝。这个过程包括用氢氧化钠在135摄氏度下消化铝土矿,因此需要蒸汽和动力。在萃取过程中,会产生大量(350m3 /h)的蒸发器和蒸发器冷凝水。考虑到现场允许的有限的液体排放,这些冷凝水被储存在现场的大池塘中,并在过程中重复使用。来自三面压力,由于水资源管理局对从井中提取原水的限制,废水的液体排放最小化的要求,以及能源成本高,需要利用蒸发器和蒸发器的再生冷凝水作为锅炉给水。国际水处理公司进行的研究得出的结论是,总有机碳(TOC)不允许冷凝水重新用作锅炉给水,并附带去除TOC的1000万美元费用。进行了大量的实验室工作和热力学分析,并将冷凝水用作锅炉给水,未经处理。节约成本为1000万美元,节约能源300万美元。
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