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应用高通量膜,以高 pH 值、脱碳酸海水为进料,降低一级反渗透的单位能耗。

Reducing the specific energy consumption of 1st-pass SWRO by application of high-flux membranes fed with high-pH, decarbonated seawater.

机构信息

Faculty of Civil and Environmental Engineering, Technion, Haifa, 32000, Israel.

Faculty of Civil and Environmental Engineering, Technion, Haifa, 32000, Israel.

出版信息

Water Res. 2015 Nov 15;85:185-92. doi: 10.1016/j.watres.2015.08.027. Epub 2015 Aug 20.

Abstract

A new operational approach is presented, which has the potential to substantially cut down on the energy and cost demand associated with seawater reverse osmosis (SWRO) desalination, without changing the currently-installed infrastructure. The approach comprises acidification/decarbonation of the feed seawater followed by high-pH single RO pass using high-flux membranes. Since the limitation imposed by CaCO3(s) precipitation is overcome, the recovery ratio can be significantly increased. This work presents a new operational concept aimed at maximizing the benefits that can be obtained from new low-energy RO membranes available on the market. Results obtained from operating a pilot RO system revealed that following an acidification and decarbonation step, recovery ratio of 56% could be practically attained, along with effluent TDS and boron concentrations of 375 and 0.3 mg/l, respectively (feed water pH was adjusted to pH9.53 following the decarbonation step). The specific energy consumption (SEC) of this operation was calculated to be 5%-10% lower than the SEC typically associated with "conventional" SWRO operation. Two further scenarios were theoretically considered, under which the limiting operational parameter became Mg(OH)2(s) and BaSO4(s) precipitation. It was concluded that despite the fact that higher recovery ratios could be obtained, the high pressure required in these scenarios made them less appealing from both the SEC and cost standpoints. The normalized cost of the suggested approach was found to be ∼$0.07 ± 0.02/m(3) cheaper than the currently-practiced SWRO approach for obtaining product water characterized by TDS < 500 and B < 0.5 mg/l.

摘要

提出了一种新的操作方法,该方法有可能在不改变当前安装的基础设施的情况下,大幅降低与海水反渗透(SWRO)脱盐相关的能源和成本需求。该方法包括对进料海水进行酸化/脱碳酸处理,然后使用高通量膜进行高 pH 值单 RO 透过。由于克服了 CaCO3(s) 沉淀的限制,可以显著提高回收率。这项工作提出了一种新的操作概念,旨在最大限度地利用市场上可用的新型低能耗 RO 膜所带来的好处。通过操作一个中试 RO 系统获得的结果表明,在酸化和脱碳酸步骤之后,可以实际达到 56%的回收率,同时出水 TDS 和硼浓度分别为 375 和 0.3 mg/l(在脱碳酸步骤之后将进料水的 pH 值调节至 pH9.53)。该操作的比能耗(SEC)比通常与“传统”SWRO 操作相关的 SEC 低 5%-10%。还从理论上考虑了另外两种情况,在这些情况下,限制操作参数是 Mg(OH)2(s) 和 BaSO4(s) 的沉淀。结论是,尽管可以获得更高的回收率,但这些情况下所需的高压使得它们从 SEC 和成本的角度来看都不那么吸引人。建议方法的归一化成本被发现比目前实践的 SWRO 方法便宜约 0.07±0.02/m(3),用于获得 TDS<500 和 B<0.5 mg/l 的产品水。

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