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利用现场中试规模的双极膜电渗析与膜气提耦合从厌氧消化池浓缩液中回收氨。

Ammonia recovery from anaerobic digester centrate using onsite pilot scale bipolar membrane electrodialysis coupled to membrane stripping.

作者信息

Ferrari Federico, Pijuan Maite, Molenaar Sam, Duinslaeger Nick, Sleutels Tom, Kuntke Philipp, Radjenovic Jelena

机构信息

Catalan Institute for Water Research (ICRA), Emili Grahit 101, 17003 Girona, Spain; University of Girona, 17003 Girona, Spain.

W&F Technologies, Noordhaven 88a, 4761 DC Zevenbergen, the Netherlands.

出版信息

Water Res. 2022 Jun 30;218:118504. doi: 10.1016/j.watres.2022.118504. Epub 2022 Apr 25.

Abstract

Ammonia recovery from centrate of an anaerobic digester was investigated using an onsite bipolar-electrodialysis (BP-ED) pilot scale plant coupled to two liquid/liquid membrane contactor (LLMC) modules. To investigate the process performance and robustness, the pilot plant was operated at varying current densities, load ratio (current to nitrogen loading), and in continuous and intermittent current (Donnan) mode. A higher load ratio led to higher total ammonium nitrogen (TAN, sum of ammonia and ammonium) removal efficiency, whereas the increase in the applied current did not have a significant impact the TAN removal efficiency. Continuous current application resulted in the higher TAN removal compared with the Donnan dialysis mode. The lowest specific energy consumption of 6.3 kWh kg was recorded in the Donnan mode, with the load ratio of 1.4, at 200 L h flowrate and current density of 75 A m. Lower energy demand observed in the Donnan mode was likely due to the lower scaling and fouling of the ion exchange membranes. Nevertheless, scaling and fouling limited the operation of the BP-ED stack in all operational modes, which had to be interrupted by the daily cleaning procedures. The LLMC module enabled a highly selective recovery of ammonia as ammonium sulfate ((NH)SO), with the concentration of ammonia ranging from 19 to 33 g L. However, the analysis of per- and polyfluoroalkyl substances (PFASs) in the obtained (NH)SO product revealed the presence of 212-253 ng L of 6:2 fluorotelomer sulfonate (FTS), a common substitute of legacy PFAS. Given the very low concentrations of 6:2 FTS (i.e., < 2 ng L) encountered in the concentrated stream, 6:2 FTS was likely released from the Teflon-based components in the sulfuric acid dosage line. Thus, careful selection of the pilot plant tubing, pumps and other components is required to avoid any risks associated with the PFAS presence and ensure safe use of the final product as fertilizer.

摘要

使用与两个液/液膜接触器(LLMC)模块相连的现场双极电渗析(BP-ED)中试规模装置,对厌氧消化器浓缩液中的氨回收进行了研究。为了研究该工艺的性能和稳健性,中试装置在不同的电流密度、负载比(电流与氮负载量之比)以及连续和间歇电流(唐南)模式下运行。较高的负载比导致总铵氮(TAN,氨和铵的总和)去除效率更高,而施加电流的增加对TAN去除效率没有显著影响。与唐南透析模式相比,连续施加电流导致更高的TAN去除率。在唐南模式下,当负载比为1.4、流量为200 L/h且电流密度为75 A/m时,记录到最低比能耗为6.3 kWh/kg。在唐南模式下观察到较低的能源需求可能是由于离子交换膜的结垢和污染较少。然而,结垢和污染限制了BP-ED堆栈在所有运行模式下的运行,必须通过每日清洗程序来中断。LLMC模块能够以硫酸铵((NH₄)₂SO₄)的形式高度选择性地回收氨,氨的浓度范围为19至33 g/L。然而,对所得(NH₄)₂SO₄产品中全氟和多氟烷基物质(PFASs)的分析表明,存在212 - 253 ng/L的6:2氟调聚物磺酸盐(FTS),这是传统PFAS的常见替代品。鉴于在浓缩物流中遇到的6:2 FTS浓度非常低(即<2 ng/L),6:2 FTS可能是从硫酸加药管线中基于特氟龙的组件中释放出来的。因此,需要仔细选择中试装置的管道、泵和其他组件,以避免与PFAS存在相关的任何风险,并确保最终产品作为肥料的安全使用。

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