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使用聚合物薄膜复合正渗透膜回收总氨氮的可行性:氨渗透系数的测定

Viability of Total Ammoniacal Nitrogen Recovery Using a Polymeric Thin-Film Composite Forward Osmosis Membrane: Determination of Ammonia Permeability Coefficient.

作者信息

Shahgodari Shirin, Llorens Joan, Labanda Jordi

机构信息

Department of Chemical Engineering and Analytical Chemistry, University of Barcelona, Martí i Franquès 1, 08028 Barcelona, Spain.

出版信息

Polymers (Basel). 2024 Jun 27;16(13):1834. doi: 10.3390/polym16131834.

Abstract

Total ammoniacal nitrogen (TAN) occurs in various wastewaters and its recovery is vital for environmental reasons. Forward osmosis (FO), an energy-efficient technology, extracts water from a feed solution (FS) and into a draw solution (DS). Asymmetric FO membranes consist of an active layer and a support layer, leading to internal concentration polarization (ICP). In this study, we assessed TAN recovery using a polymeric thin-film composite FO membrane by determining the permeability coefficients of NH and NH. Calculations employed the solution-diffusion model, Nernst-Planck equation, and film theory, applying the acid-base equilibrium for bulk concentration corrections. Initially, model parameters were estimated using sodium salt solutions as the DS and deionized water as the FS. The NH permeability coefficient was 0.45 µm/s for NHCl and 0.013 µm/s for (NH)SO at pH < 7. Meanwhile, the NH permeability coefficient was 6.18 µm/s at pH > 9 for both ammonium salts. Polymeric FO membranes can simultaneously recover ammonia and water, achieving 15% and 35% recovery at pH 11.5, respectively.

摘要

总氨氮(TAN)存在于各种废水中,出于环境原因,其回收至关重要。正向渗透(FO)是一种节能技术,可将水从进料溶液(FS)中提取到汲取溶液(DS)中。非对称FO膜由活性层和支撑层组成,会导致内部浓差极化(ICP)。在本研究中,我们通过测定NH₃和NH₄⁺的渗透系数,使用聚合物薄膜复合FO膜评估了TAN的回收情况。计算采用了溶液扩散模型、能斯特-普朗克方程和膜理论,并应用酸碱平衡进行本体浓度校正。最初,使用钠盐溶液作为DS,去离子水作为FS来估计模型参数。在pH < 7时,NH₄Cl的NH₃渗透系数为0.45 µm/s,(NH₄)₂SO₄的为0.013 µm/s。同时,在pH > 9时,两种铵盐的NH₄⁺渗透系数均为6.18 µm/s。聚合物FO膜可同时回收氨和水,在pH 11.5时分别实现15%和35%的回收率。

https://cdn.ncbi.nlm.nih.gov/pmc/blobs/83d8/11244275/83d6e4e1b115/polymers-16-01834-g001.jpg

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