Synthesis of methyl 3,5-diaminobenzoate to develop polyamide thin film composite membrane for investigating the impact of in-situ methyl hydrolysis on its permeate flux and sulfate rejection

IF 9 1区 工程技术 Q1 ENGINEERING, CHEMICAL Separation and Purification Technology Pub Date : 2025-02-23 DOI:10.1016/j.seppur.2025.132178
Umair Baig , Abdul Waheed , Hilal Ahmad , Isam H. Aljundi
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Abstract

The performance of the desalination membranes has been improved by exploiting the potential of interfacial polymerization by using different combinations of reacting monomers. However, for successful interfacial polymerization, the aqueous amine must diffuse to the organic phase resulting in polyamide growth. Owing to that stringent requirement, using an essential amine 3,5-diaminobenzoic acid (DABA) for membrane fabrication in the literature has not been successful. The 3,5-diaminobenzoic acid is an analog of meta-phenylenediamine with an additional carboxylic group on the benzene ring. The presence of an additional carboxylic group in the case of 3,5-diaminobenzoic acid makes it attractive to develop a membrane with additional carboxylic groups in the active layer of the membrane. However, this carboxylic group hinders the diffusion of the 3,5-diaminobenzoic acid during interfacial polymerization, hence no appreciable growth of polyamide active layer. The current study resolved this challenge by masking the carboxylic group through methyl esterification yielding a methyl-ester-containing version N-DABA. When used during interfacial polymerization, the N-DABA yielded a dense polyamide active layer. To take advantage of the additional carboxylic group of 3,5-diaminobenzoic acid, the methyl ester group was partially hydrolyzed using an in-situ basic hydrolysis approach. Hence, two variants of membranes were fabricated in the current study, N-DABA/TMC and m-N-DABA/TMC membrane, and several desalination experiments were performed. The desalination experiments revealed that the membranes possessed preferential rejection of SO42− ions (Na2SO4) reaching around 96% for the N-DABA/TMC membrane with a permeate flux of around 25.7 L m−2 h−1 at 20 bar. In the case of m-N-DABA/TMC membrane, a rejection of around 94.7% was recorded for Na2SO4. However, a significant enhancement of nearly 2 folds was recorded in the permeate flux reaching around 51.4 L m−2 h−1 at 20 bar. Moreover, the membranes showed a significant enhancement in the antifouling properties by achieving normalized fluxes of 0.88 and 0.73 for the N-DABA/TMC and m-N-DABA/TMC membranes, respectively.

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合成3,5-二氨基苯甲酸甲酯制备聚酰胺薄膜复合膜,研究原位甲基水解对其渗透通量和硫酸盐截留性能的影响
通过使用不同的反应单体组合,利用界面聚合的潜力,海水淡化膜的性能得到了改善。然而,要成功实现界面聚合,水胺必须扩散到有机相中,导致聚酰胺的生长。由于这一严格要求,文献中使用必需胺 3,5-二氨基苯甲酸(DABA)制造膜的方法并不成功。3,5-二氨基苯甲酸是一种在苯环上带有额外羧基的间苯二胺类似物。由于 3,5-二氨基苯甲酸含有一个额外的羧基,因此开发一种在膜的活性层中含有额外羧基的膜很有吸引力。然而,在界面聚合过程中,这种羧基阻碍了 3,5-二氨基苯甲酸的扩散,因此聚酰胺活性层没有明显增长。目前的研究通过甲基酯化掩盖羧基,得到了含甲基酯的 N-DABA,从而解决了这一难题。在界面聚合过程中使用 N-DABA 时,可生成致密的聚酰胺活性层。为了利用 3,5-二氨基苯甲酸的额外羧基,采用原位碱性水解法对甲酯基团进行了部分水解。因此,本研究制作了两种膜,即 N-DABA/TMC 膜和 m-N-DABA/TMC 膜,并进行了多次脱盐实验。海水淡化实验表明,N-DABA/TMC 膜对 SO42- 离子(Na2SO4)的优先排斥率约为 96%,在 20 巴压力下的渗透通量约为 25.7 L m-2h-1。在 m-N-DABA/TMC 膜中,Na2SO4 的抑制率约为 94.7%。然而,在 20 巴压力下,渗透通量大幅提高了近 2 倍,达到约 51.4 L m-2h-1。此外,N-DABA/TMC 膜和 m-N-DABA/TMC 膜的防污性能也有显著提高,归一化通量分别达到 0.88 和 0.73。
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来源期刊
Separation and Purification Technology
Separation and Purification Technology 工程技术-工程:化工
CiteScore
14.00
自引率
12.80%
发文量
2347
审稿时长
43 days
期刊介绍: Separation and Purification Technology is a premier journal committed to sharing innovative methods for separation and purification in chemical and environmental engineering, encompassing both homogeneous solutions and heterogeneous mixtures. Our scope includes the separation and/or purification of liquids, vapors, and gases, as well as carbon capture and separation techniques. However, it's important to note that methods solely intended for analytical purposes are not within the scope of the journal. Additionally, disciplines such as soil science, polymer science, and metallurgy fall outside the purview of Separation and Purification Technology. Join us in advancing the field of separation and purification methods for sustainable solutions in chemical and environmental engineering.
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