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Membranes are important in the pharmaceutical industry for the separation of antibiotics and salts. However, its widespread adoption has been hindered by limited control of the membrane microstructure (pore architecture and free‐volume elements), separation threshold, scalability, and operational stability. In this study, 4,4′,4′′,4′′′‐methanetetrayltetrakis(benzene‐1,2‐diamine) (MTLB) as prepared as a molecular building block for fabricating thin‐film composite membranes (TFCMs) via interfacial polymerization. The relatively large molecular size and rigid molecular structure of MTLB, along with its non‐coplanar and distorted conformation, produced thin and defect‐free selective layers (~27 nm) with ideal microporosities for antibiotic desalination. These structural advantages yielded an unprecedented high performance with a water permeance of 45.2 L m−2 h−1 bar−1 and efficient antibiotic desalination (NaCl/adriamycin selectivity of 422). We demonstrated the feasibility of the industrial scaling of the membrane into a spiral‐wound module (with an effective area of 2.0 m2). This module exhibited long‐term stability and performance that surpassed those of state‐of‐the‐art membranes used for antibiotic desalination. This study provides a scientific reference for the development of high‐performance TFCMs for water purification and desalination in the pharmaceutical industry. [ABSTRACT FROM AUTHOR]

Based on a mutual internal relationship among membrane properties (e.g., permeability, selectivity, antifouling ability), a comprehensive performance improvement of the thin film composite (TFC) membrane remains the huge issue. In this study, single walled carbon nanotube (SWCNT) was used as a nanofiller to tune the polyester membrane via the IP reaction with carboxymethyl cellulose (CMC) and TMC as aqueous and organic monomer, respectively. Through Van der Waals interaction and hydrogen bonding with SWCNT, the diffusion behavior of CMC towards the TMC boundary was affected and finally tune the properties and structures of the polyester active layer. Besides, physical and chemical natures of the fabricated membranes modified by different SWCNT concentrations were characterized. The results revealed that polyester selective layer presented a rougher and more hydrophilic surface with an increased content, which were beneficial for water molecules transit. Consequently, the optimal TFC membrane decorated by 0.50 mg SWCNT presented an excellent permeance at 14.47 L m−2 h−1 bar−1 and satisfied dye retention of 99.7%, 100.0%, 100.0%, and 98.0% for congo red, coomassie blue G250, reactive blue 19, and methyl blue, respectively. Moreover, TFC membrane exhibited moderate salt rejections against Na2SO4 (91.8%), MgSO4 (23.2%), NaCl (24.3%), and MgCl2 (2.9%) and preferable long-term filtration stability of 72 h, which was rather competitive for the application of wastewater treatment. [ABSTRACT FROM AUTHOR]

Covalent organic framework (COF) membranes featuring uniform topological structures and devisable functions, show huge potential in water purification and molecular separation. Nevertheless, the inability of uniform COF membranes to be produced on an industrial scale and their nonenvironmentally friendly fabrication method are the bottleneck preventing their industrial applications. Herein, we report a new green and industrially adaptable scraping‐assisted interfacial polymerization (SAIP) technique to fabricate scalable and uniform TpPa COF membranes. The process used non‐toxic and low‐volatility ionic liquids (ILs) as organic phase instead of conventional organic solvents for interfacial synthesis of TpPa COF layer on a support membrane, which can simultaneously achieve the purposes of (i) improving the greenness of membrane‐forming process and (ii) fabricating a robust membrane that can function beyond the conventional membranes. This approach yields a large‐area, continuous COF membrane (19×25 cm2) with a thickness of 78 nm within a brief period of 2 minutes. The resulting membrane exhibited an unprecedented combination of high permeance (48.09 L m−2 h−1 bar−1) and antibiotic desalination efficiency (e.g., NaCl/adriamycin separation factor of 41.8), which is superior to the commercial benchmarking membranes. [ABSTRACT FROM AUTHOR]

Inspired by biological membranes with charge-gated channels that allow the transport of water and ions but restrict the undesired substances, various regulated nanofiltration (NF) membranes containing charge-gated channels have been developed for water purification. However, most of these membranes are mono-charged (positively or negatively) that show high rejection only to the corresponding co-ions but low rejection to the counter-ions, which limits their wider applications. Herein, we report NF membranes with gas-tunable charge-gated channels and high rejection to different salts on demand. The membranes are prepared by assembling a CO 2 -responsive polymer, poly(N,N-dimethylaminoethyl methacrylate), on the surface of graphene oxide (GO). As a result of CO 2 -induced reversal of the charge sign, the membranes exhibit "self-regulation" of their surface charges. Upon bubbling CO 2 into water, the membranes are positively charged, which shows high rejection to MgCl 2. After bubbling Ar to remove CO 2 , the membranes gradually transform to negatively charged, and high rejection to Na 2 SO 4 is obtained. This study demonstrates the gas-tunable charge-gated ion transport behavior of the CO 2 -responsive NF membranes, and opens up new avenues for the design of on-demand NF membranes. New nanofiltration membranes exhibit on-demand switchable rejections toward cations and anions with the participation and departure of CO 2. Image 1 • New nanofiltration membrane was built with graphene oxide and CO 2 -responsive polymer. • The surface of nanopores can be reversibly switched between opposite charged state. • Charge sign can easily be reversed in a robust and contamination-free manner. • Ion transport behavior was dominated with the participation and departure of CO 2. [ABSTRACT FROM AUTHOR]