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A novel approach for SWRO desalination plants operation, comprising single pass boron removal and reuse of CO2 in the post treatment step

机译:SWRO海水淡化厂运行的新方法,包括在处理后步骤中单程除硼和再利用CO2

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A different approach is presented for the operation of seawater RO desalination plants in which the boron concentration in the product water should not exceed 0.3 mgB/l. The approach is based on strong acid (either H2SO4 or HCl) dosage to the feed water to attain pH~4.3, followed by CO2 stripping and subsequently strong base addition to pH 9.00-9.25. At this high pH range, a high B removal efficiency is attained, and since the water is practically devoid of carbonate species, no CaCO_(3(s)) scaling takes place, and pH elevation is limited by Mg(OH)_(2(s)) precipitation, expected only at pH > 9.45. The approach enables operation in the absence of antiscalants. Furthermore, CO2 stripping is effected in stripping towers in two steps: the high CO_(2(aq)) concentration is first stripped by vacuum-operated stripping towers and the CO2-rich air is used for dissolution of calcite in the post treatment stage. The remaining CO2 mass is stripped to the atmosphere using blower-assisted stripping towers. This paper aims at introducing the new concept and providing "proof of concept". The paper addresses experimental and theoretical aspects of the proposed process, as well as engineering and economic evaluation. The proposed approach is shown to be both technically feasible and cost effective, as compared with conventional boron removal alternatives.
机译:对于海水反渗透淡化厂的运行,提出了一种不同的方法,其中产品水中的硼浓度不应超过0.3 mgB / l。该方法是基于给水中加入强酸(H2SO4或HCl)以达到pH〜4.3,然后进行CO2汽提,然后再加入强碱至pH 9.00-9.25。在此高pH范围内,可获得较高的B去除效率,并且由于水实际上不含碳酸盐物种,因此不会发生CaCO_(3(s))结垢,并且pH升高受Mg(OH)_(2 (s))沉淀,仅在pH> 9.45时才预期。该方法能够在不存在防垢剂的情况下进行操作。此外,在汽提塔中分两步进行二氧化碳汽提:首先通过真空汽提塔汽提高浓度的CO_(2(aq)),然后在后处理阶段将富含二氧化碳的空气用于方解石的溶解。使用鼓风机辅助的汽提塔将剩余的CO2物料汽提到大气中。本文旨在介绍新概念并提供“概念证明”。本文介绍了拟议流程的实验和理论方面,以及工程和经济评估。与传统的除硼替代品相比,所提出的方法在技术上既可行又具有成本效益。

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