4.7 Article

High separation performance thin film composite and thin film nanocomposite hollow fiber membranes via interfacial polymerization for organic solvent nanofiltration

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ELSEVIER
DOI: 10.1016/j.seppur.2021.119567

关键词

Hollow fiber (HF) membrane; Organic solvent nanofiltration (OSN); Interfacial polymerization; Thin film composite (TFC); Thin film nanocomposite (TFN)

资金

  1. National Natural Science Foundation of China [22078310]
  2. Fundamental Research Funds for the Central Universities of China [201822012]
  3. Key Project Fund of Science and Technology of Shandong Province [2019GGX102040]

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HF organic solvent nanofiltration membranes have a unique structure and high surface area, suitable for separation intensification in chemical industries. Controlling the additives and solution concentration can lead to high-performance HF OSN membranes, and incorporating graphene oxide can improve ethanol permeance.
Hollow fiber (HF) organic solvent nanofiltration (OSN) membrane has unique self-supporting structure and larger specific surface area over flat OSN membranes, which is much more beneficial for separation processes intensification in chemical related industries. The key of this technology is HF OSN membrane. However, the research works on HF OSN membranes was relatively less till now. In this work, an outer-skinned polyimide HF substrate membrane was spun, and then thin film composite (TFC) membrane was prepared via interfacial polymerization (IP) between ultra-low concentration m-phenylenediamine (MPD) in the aqueous phase and trimesoyl chloride (TMC) in the organic phase on the HF substrate surface, with sodium dodecyl sulfate (SDS) as aqueous additives and triethylamine (TEA) as aqueous catalyst, and subsequently accompanied by crosslinking and solvent activation procedures. Further, thin film nanocomposite (TFN) HF OSN membrane incorporated with graphene oxide (GO) was also prepared. The combination of lower MPD concentration with SDS and TEA as additives in the aqueous monomer solution promote the formation of a TFC HF OSN membrane with average roughness of less than 3 nm, and a rhodamine B (RDB) rejection close to 100%, together with an ethanol permeance higher than 12 L m(-2) h(-1) MPa-1 under the optimum fabrication conditions. The optimal TFN membrane at a doping GO content of 5.0 mg L-1 achieves up to 20 L m(-2) h(-1) MPa-1 for the ethanol permeance without sacrificing the RDB rejection (nearly 100%). Moreover, both HF OSN membranes possess good swelling resistance, which proves their application potential in organic solvent system.

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